U.S. patent application number 11/004669 was filed with the patent office on 2005-11-24 for decontamination methods for meat using carbonic acid at high pressures.
Invention is credited to Garwood, Anthony J.M..
Application Number | 20050260311 11/004669 |
Document ID | / |
Family ID | 35375455 |
Filed Date | 2005-11-24 |
United States Patent
Application |
20050260311 |
Kind Code |
A1 |
Garwood, Anthony J.M. |
November 24, 2005 |
Decontamination methods for meat using carbonic acid at high
pressures
Abstract
A method for separating lean meat from lean meat-containing
material, includes combining a particulate material with fluid,
subcritical carbon dioxide at a pH of about 7 or less and a
pressure of about 600 psig. The material and fluid is introduced
into the vessel and is separated into low density and high density
fractions. The material from the low density fraction is removed
via an outlet and has a higher percentage of fat than the material
introduced into the vessel. The material from the high density
fraction is removed via an outlet and has a higher percentage of
lean meat than the material introduced into the vessel. The vessel
can include a centrifuge or a vessel disposed toward the vertical
having an upper and lower outlet, wherein the separation is
achieved by the respective densities of the material, and the
natural or an artificial gravity field, such as in a
centrifuge.
Inventors: |
Garwood, Anthony J.M.;
(Mercer Island, WA) |
Correspondence
Address: |
CHRISTENSEN, O'CONNOR, JOHNSON, KINDNESS, PLLC
1420 FIFTH AVENUE
SUITE 2800
SEATTLE
WA
98101-2347
US
|
Family ID: |
35375455 |
Appl. No.: |
11/004669 |
Filed: |
December 2, 2004 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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11004669 |
Dec 2, 2004 |
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PCT/US03/17643 |
Jun 3, 2003 |
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60385710 |
Jun 3, 2002 |
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60388067 |
Jun 10, 2002 |
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60391702 |
Jun 24, 2002 |
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60411138 |
Sep 16, 2002 |
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60422949 |
Oct 30, 2002 |
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60424388 |
Nov 5, 2002 |
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60427516 |
Nov 19, 2002 |
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60429644 |
Nov 25, 2002 |
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60433526 |
Dec 13, 2002 |
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60438546 |
Jan 7, 2003 |
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Current U.S.
Class: |
426/480 |
Current CPC
Class: |
A23B 4/24 20130101; A23J
1/02 20130101; A23B 4/20 20130101; A23V 2002/00 20130101; A23V
2250/11 20130101; A23V 2200/10 20130101; A23B 4/16 20130101; A23L
5/20 20160801; A23L 13/00 20160801; A23L 3/0155 20130101; A23V
2002/00 20130101; A23B 4/26 20130101 |
Class at
Publication: |
426/480 |
International
Class: |
A23L 001/27 |
Claims
1. A method for separating lean meat from lean meat-containing
material, comprising; combining a particulate material having lean
meat and fat with a fluid comprising subcritical carbon dioxide,
wherein the combination of the material with the fluid has a pH of
about 7 or less; introducing the material and fluid into a vessel
to fill the vessel, wherein the vessel has first and second
outlets, and allowing the material to separate into low density and
high density fractions within sections of the vessel; removing
material from the low density fraction via the first outlet of the
vessel, wherein the material removed from the first outlet has a
higher percentage of fat than the material introduced into the
vessel; and removing material from the high density fraction via
the second outlet of the vessel, wherein the material removed from
the second outlet has a higher percentage of lean meat than the
material introduced into the vessel.
2. The method of claim 1, wherein the density of the fluid is
adjusted by the addition of water.
3. The method of claim 1, wherein the density of the fluid is
increased by the addition of water and sodium chloride.
4. The method of claim 1, further comprising grinding the material
prior to combining with the fluid.
5. The method of claim 1, further comprising adjusting the
temperature of the material prior to combining with the fluid to a
temperature of about 28.degree. F. to about 109.degree. F. and
adjusting the pressure to lower than 600 psig.
6. The method of claim 1, further comprising extracting the
material removed from the low density fraction of the first vessel,
introducing the extracted material into a second vessel having a
first outlet and a second outlet, allowing the material to separate
into low density and high density fractions within sections of the
second vessel, removing material from the low density fraction via
the first outlet of the second vessel, wherein the material removed
from the first outlet has a higher percentage of fat than the
material introduced into the second vessel; and removing material
from the high density fraction via the second outlet of the second
vessel, wherein the material removed from the second outlet has a
higher percentage of lean meat than the material introduced into
the second vessel.
7. The method of claim 1, further comprising separating fluid from
the low density fraction.
8. The method of claim 1, further comprising separating fluid from
the high density fraction.
9. The method of claim 1, wherein the vessel comprises an inlet at
about the midsection of the vessel, and the material and fluid are
introduced at the inlet at about the midsection of the vessel.
10. The method of claim 1, further comprising separating fluid from
the material in the low density fraction, separating fluid from the
material in the high density fraction, and recycling the separated
fluid to combine with material.
11. The method of claim 1, further comprising processing material
having lean meat and fat in a centrifuge.
12. The method of claim 1, further comprising measuring the carbon
dioxide combined with the material to maintain a ratio of about
one-half to four times the flow rate of the material.
13. The method of claim 1, further comprising removing fluid from
the vessel that is about equal to the amount of fluid that is
combined with the material.
14. The method of claim 1, further comprising introducing an agent
from at least one of sodium chloride, sodium chlorite, carbon
monoxide and sodium citrate.
15. The method of claim 1, wherein the material removed from the
high density fraction is identified with one or more animals from
which material originated.
16. A method for separating fat from material containing lean meat
and fat, comprising: introducing a material containing lean meat
and fat to a conduit containing a rotating and tapering transfer
mechanism; introducing carbon dioxide to the conduit at a pressure
and temperature below the critical temperature and critical
pressure for carbon dioxide; transferring the material and carbon
dioxide along the conduit by rotating the tapering transfer
mechanism; separating carbon dioxide with fat through an outlet
disposed along the conduit to produce material product containing a
lower percentage of fat than the material introduced into the
conduit.
17. The method of claim 16, further comprising measuring the fat
and moisture content of the material prior to introducing to the
conduit, and optionally introducing carbon dioxide at a controlled
pressure and a measured proportion of water to adjust the moisture
content of the material.
18. The method of claim 16, further comprising introducing an agent
from at least one of sodium chloride, sodium chlorite, carbon
monoxide and sodium citrate.
19. The method of claim 16, wherein the material product is
identified with one or more source animals from which material
originated.
20. The method of claim 19 wherein the identification of at least
one source animal is attached to the meat after processing.
Description
CROSS-REFERENCES TO RELATED APPLICATIONS
[0001] This application is a continuation-in-part of
PCT/US03/17643, filed Jun. 3, 2003, which claims the benefit of
U.S. Provisional Application Nos. 60/385,710, filed Jun. 3, 2002;
60/388,067, filed Jun. 10, 2002; 60/391,702, filed Jun. 24, 2002;
60/411,138, filed Sep. 16, 2002; 60/422,949, filed Oct. 30, 2002;
60/424,388, filed Nov. 5, 2002; 60/427,516, filed Nov. 19, 2002;
60/429,644, filed Nov. 25, 2002; 60/433,526, filed Dec. 13, 2002;
60/438,546, filed Jan. 7, 2003. All the above applications are
herein expressly incorporated by reference.
FIELD OF THE INVENTION
[0002] The present invention relates to the decontamination of any
goods, solid or liquid, including meat, with the use of carbon
dioxide at high pressure.
BACKGROUND OF THE INVENTION
[0003] At a time when there is increasing consumer demand for
natural, and if possible organic, foods, and an increasing
regulatory requirement for the reduction or elimination of
artificial chemicals and preservatives; it is alarming to note that
many proposed methods for decontaminating meat rely on the addition
of chemicals not normally found in such foods.
[0004] One such food is a beef product known as Lean Fine Textured
Beef (hereinafter "LFTB"). LFTB can be harvested from discarded
"fat" cut from carcasses. During the process of boning a carcass,
the external fat layer can be removed. During the process, a
significant amount of lean meat can be cut from the carcass and
discarded with the fat. To recover the lean meat, the discarded fat
can be heated to about 109.degree. F. The heated fat can be
processed in a centrifuge that separates the fat from the lean
meat. The lean meat is then frozen and chipped into small flakes.
The finished product, known as LFTB, is then stored in a frozen
condition and can later be added to ground beef, for example. The
temperature of the LFTB during the separation process does not
exceed the temperature that a carcass would normally experience
post mortem. As a result, pathogens and bacteria that are present
on the surfaces of the carcass prior to boning can result in
bacteria being present in the LFTB.
[0005] A need exists to more effectively kill, reduce or remove the
microbial population on any processed meat, or any other good,
liquid or solid, to eliminate sources of cross contamination and
recontamination, while simultaneously allaying the concerns of
using artificial chemicals. A need also exists to more effectively
separate fat from lean meat.
SUMMARY OF THE INVENTION
[0006] A method for separating lean meat from lean meat-containing
material, includes combining a particulate material having lean
meat and fat with fluid, subcritical carbon dioxide at a pH of
about 7 or less. The material and fluid is introduced into a
vessel. The material is separated into low density and high density
fractions within sections of the vessel. The material from the low
density fraction is removed via a first outlet, and the material
removed via the first outlet has a higher percentage of fat than
the material introduced into the vessel. The material from the high
density fraction is removed via a second outlet, and the material
removed via the second outlet has a higher percentage of lean meat
than the material introduced into the vessel. The vessel can
include a centrifuge or a vessel disposed toward the vertical
having an upper and lower outlet, wherein the separation is
achieved by the force of the natural or an artificially created
gravity field, such as in a centrifuge, acting on the material, and
the fractions are formed based on the respective densities of the
material. The separation may be carried out at elevated pressures,
such as at a maximum of about 600 psig, or about 500 psig.
[0007] The density of the fluid can be controlled, and can either
be increased or decreased to control the separation. The particle
size of the material effects the efficiency of separation, since
the smaller the particles, the more likely that the particle will
be either mostly lean meat or mostly fat. For example, larger
particles may have just enough of a majority of either lean meat or
fat to separate in one direction or the other. As the particles are
reduced in size, each individual particle will have a greater
majority of either lean meat or fat, and will tend to separate
quicker. At the very extreme, when particles are reduced to the
molecular level, each particle will be either all lean or all
fat.
[0008] In one embodiment, the fat content of the processed ground
beef is determined by particle size, for example, by reducing the
particle size, separation will be more thorough, and the lean meat
will be lower in fat content. Therefore, the fat content of the
lean meat product can be determined by controlling the particle
size. The larger the particle, the more fat will be retained in the
lean meat stream, and the smaller the particle, the less fat will
be retained in the lean meat stream. The density of the fluid can
also be manipulated to effect the separation efficiency.
[0009] One embodiment of the present invention is directed to a
method and apparatus for decontaminating goods, such as meat, by
using a "shock" method (hereinafter AST) involving immersion of
meat in a high pH alkaline solution followed by immersion in a low
pH acid, such as carbon dioxide and water at higher than
atmospheric pressures. Alternatively, the method can incorporate
irradiation of meat.
[0010] In one embodiment, a decontamination method for goods, such
as meat, is disclosed that exposes the goods to a low pH followed
by exposure to irradiation, such as x-ray, gamma, or e-beam.
[0011] In one embodiment of the invention, the high pH solution can
include calcium and hydroxide ions.
[0012] In one embodiment of the invention, high pH alkali such as
calcium hydroxide solution is sprayed onto meat portions in a
manner so as to ensure a substantially complete covering of the
outer surfaces of the meat. The pH at the surface of the meat is
elevated to a pH of about 12 to about 14. The bacteria is subjected
to the high pH and is either killed by the high pH or becomes
acclimatized to it. After the meat has been exposed to high pH
conditions for an effective period of time, the meat can then be
immersed in a low pH acid, such as can be provided with blending
carbon dioxide and water at a suitable temperature and pressure.
High pressure causes the formation of carbonic acid. The
probability of killing bacteria is almost certain since the rapid
change of pH from about 12 to about 3 shocks the bacteria and are
unable to acclimatize to the rapid pH change. Such microorganisms
killed may be E. coli 0157:H7, Salmonella, Listeria monocytogenes,
and other pathogens.
[0013] In another embodiment, an alkali metal chlorite is added,
either as a solid or in solution, to the meat that is to be
decontaminated, prior to exposure of the meat to an acid, such as
carbonic acid, that is generated by dissolving carbon dioxide in
water at a suitable high pressure to cause a lowering of the pH.
The benefit of applying an alkali metal chlorite prior to addition
of the acid and not with the acid is that the alkali metal chlorite
is not wasted prior to the time when it is needed. Applying a
solution of a chlorite together with an acid will result in a waste
of sodium chlorite. Representative alkali metals include potassium
and sodium.
[0014] The microbiocidal effect is noticeable at acidic pH values
below about 7.0 and more pronounced below about 4.0. The
microbiocidal effect is maximized when the pH of the alkaline
solution is about 12 to about 14 and is followed by immersion in a
solution of dissolved carbon dioxide in water such that the pH of
carbonic acid is less than 7, or about 2 to about 3.
[0015] In another embodiment, the surface of the meat can be kept
substantially at about 28.degree. F. to about 40.degree. F. to
avoid freezing. Chilling of the meat can be accomplished by using
the carbon dioxide in a form that provides substantial latent heat
of evaporation such as a dense gas, liquid or solid.
[0016] Exposure of meat to oxygen can produce undesirable brown
color in meat due to oxidation. It is therefore desirable to
substantially prevent oxygen from contacting goods, such as meat.
Eliminating the presence of oxygen as much as possible during
processing, handling, storage and packaging can produce meat having
an extended storage or shelf life.
[0017] In another aspect of the present invention, a process to
reduce bacteria, including E. coli 0157: H7 and other bacteria and
pathogens, to a level within desirable limits, while also
simultaneously controlling the water content in meat and adjusting
the fat content in meat, is provided. Furthermore, beef trim that
has been removed from beef cuts and carcasses during the normal
process of disassembly and is either presently disposed of by
rendering, or alternatively processed by Beef Producers of Iowa
(hereinafter "BPI") to produce a product known as lean finely
textured beef (hereinafter "LFTB"), can be processed according to
the invention.
[0018] In another aspect of the present invention, apparatus are
provided to carry out methods for decontaminating meat of pathogens
using carbon dioxide.
BRIEF DESCRIPTION OF THE DRAWINGS
[0019] The foregoing aspects and many of the attendant advantages
of this invention will become more readily appreciated as the same
become better understood by reference to the following detailed
description, when taken in conjunction with the accompanying
drawings, wherein:
[0020] FIG. 1 shows a block diagram of a process according to the
present invention;
[0021] FIG. 2 shows a schematic illustration of an apparatus
according to the present invention;
[0022] FIG. 3 shows a schematic illustration of an apparatus
according to the present invention;
[0023] FIG. 4 shows a schematic illustration of an apparatus
according to the present invention;
[0024] FIG. 5 shows a schematic illustration of an apparatus
portion according to the present invention;
[0025] FIG. 6 shows a schematic illustration of an apparatus
according to the present invention;
[0026] FIG. 7 shows a schematic illustration of an apparatus
according to the present invention;
[0027] FIG. 8 shows a schematic illustration of an apparatus
according to the present invention;
[0028] FIG. 9 shows a schematic illustration of a valve according
to the present invention;
[0029] FIG. 10 shows a schematic illustration of an apparatus
according to the present invention;
[0030] FIG. 11 shows a schematic cross-sectional illustration of an
apparatus portion according to the present invention;
[0031] FIG. 12 shows a schematic illustration of a cage according
to the present invention;
[0032] FIG. 13 shows a cross-sectional illustration of the cage of
FIG. 12;
[0033] FIG. 14 shows a cross-sectional illustration of the cage of
FIG. 12;
[0034] FIG. 15 shows a cross-sectional illustration of the cage of
FIG. 12;
[0035] FIG. 16 shows a cross-sectional illustration of the cage of
FIG. 12;
[0036] FIG. 17 shows a schematic illustration of a cage according
to the present invention;
[0037] FIG. 18 shows a cross-sectional illustration of the cage of
FIG. 17;
[0038] FIG. 19 shows a cross-sectional illustration of the cage of
FIG. 17;
[0039] FIG. 20 shows a cross-sectional illustration of the cage of
FIG. 17;
[0040] FIG. 21 shows a cross-sectional illustration of the cage of
FIG. 17;
[0041] FIG. 22 shows a cross-sectional illustration of mated cages
of FIG. 17;
[0042] FIG. 23 shows a schematic illustration of an apparatus
according to the present invention;
[0043] FIG. 24 shows a schematic illustration of an apparatus
according to the present invention;
[0044] FIG. 25 shows a schematic illustration of an apparatus
according to the present invention;
[0045] FIG. 26 shows a schematic illustration of an apparatus
according to the present invention;
[0046] FIG. 27 shows a mobile apparatus according to the present
invention;
[0047] FIG. 28 shows a cross-sectional illustration of a mobile
apparatus unit according to the present invention;
[0048] FIG. 29 shows a block diagram of one embodiment of a method
according to the present invention;
[0049] FIG. 30 shows a schematic illustration of an apparatus
according to the present invention;
[0050] FIG. 31 shows a schematic illustration of an apparatus
according to the present invention;
[0051] FIG. 32 shows a schematic illustration of an apparatus
according to the present invention;
[0052] FIG. 33 shows a schematic illustration of an apparatus
according to the present invention;
[0053] FIG. 34 shows a cross sectional illustration of the
apparatus of FIG. 33;
[0054] FIG. 35 is an illustration of one embodiment of an apparatus
according to the present invention;
[0055] FIG. 36 shows a schematic illustration of an apparatus
according to the present invention;
[0056] FIG. 37 shows a schematic illustration of an apparatus
according to the present invention;
[0057] FIG. 38 shows a schematic illustration of an apparatus
according to the present invention;
[0058] FIG. 39 shows a schematic illustration of an apparatus
according to the present invention;
[0059] FIG. 40 shows a schematic illustration of an apparatus
according to the present invention; and
[0060] FIG. 41 shows a schematic illustration of an apparatus
according to the present invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0061] The decontamination, pasteurization, and processing
apparatus and methods described below can be for goods, such as
meat, boneless or otherwise, with the optional use of any
additional substance(s), liquid(s) and/or gas(es), which use carbon
dioxide and water in any selected, relative, and/or measured
quantities and at any suitable pressure, combined together in an
effective manner so as to produce carbonic acid. Additionally, the
water (moisture) content of the goods, such as beef or poultry
meats, can be measured and controlled according to the methods
disclosed.
[0062] One aspect of the invention provides water content standards
for meat. The water content standards can be used to approximate
the naturally occurring level of moisture in any meat. The
composition of fresh boneless meat, harvested from an animal, can
be reduced to substantially two components, lean meat, and fat.
Both lean meat and fat can contain a large percentage of water. A
more extensive analysis of meat, harvested from any animal used as
food intended for human consumption, can include elements such as
hydrogen, oxygen, carbon, and metals such as iron, calcium, sodium
and potassium. Elements that comprise the meat harvested from the
animal can be measured and stored in a computerized system and
database that can be accessed for the beneficial evaluation of the
data and also to establish water content standards for meat
composition to enable the definition of limitations of any
particular element or compound that can cause harm to any human
that may consume the meat. For example, limits of the metal mercury
are already established. Water can represent the largest single
component by weight of the meat or fat. Water can evaporate readily
when exposed to air, and particularly when exposed to refrigerated
air. Water loss in refrigerated air may be as much as about 1% to
about 2% for every 24-hour period when the fresh meat is exposed to
the refrigerated air. Water loss can occur throughout the duration
of meat processing. Water loss can represent a significant loss,
and thus reduce profits. Accordingly, it is desirable to avoid
and/or control the water content in meats. The present invention
can provide methods for the control of the water content in
meats.
[0063] The present invention provides a method that includes
measuring the water content of fresh meats harvested from animals.
The data derived from the measurements can be transferred to a
computerized database for use in developing a set of water content
standards (standards) that can provide the water composition for
any meat from any group of animals that are related by one or more
characteristics. The standards can then be used as a reference to
control the water content at any given level of meat harvested from
an animal belonging to the corresponding group or category, even
when the water content of the meat is not directly measured. The
standards are derived from data previously obtained from different
animals constituting the same group of animals as the animal from
which the meat was harvested.
[0064] In order to enable the continued improvement and accuracy of
the standards, the data can be integrated and/or transferred
between several databases that are used in the meat production
industries. In particular, a corporation known as Global Animal
Management, Inc., (hereinafter "GAM") has developed a system
enabling the collection and storage of data associated with, for
example, genetics, ancestry, birth, lifespan, food consumption,
food conversion efficiencies, medications, and growth
characteristics. The GAM system can evaluate the performance of
medications and any variations in performance. Solutions can be
found and problems resolved that otherwise may never have been
identified. The GAM database can be directly interfaced or
integrated with the standards database according to the invention,
to enable the evaluation of other factors that will enable
resolution of problems. Another company called Systems Integration
Trading, Limited, (hereinafter "SITL") provides equipment and
methods that can be incorporated with the present standards
database of the invention. Additionally, a corporation based in
Germany and known as E+V Technology GmbH, (hereinafter "EVT") has
developed a carcass grading and classification system. The EVT
system uses data acquired from a single digital image to determine
the size, weight, conformation and other qualities of an animal
carcass. The accuracy and speed of the EVT system is vastly more
accurate and efficient than the corresponding accuracy and
productivity of data and measurements acquired manually with human
labor. Data and measurements are accumulated in the database over a
period of time, and wide variations in carcass data enables rapid
classification of every carcass. This is achieved by comparing the
data acquired from the digital image of the carcass with the
historical data which establishes the "best fit" and then
classifies the carcass to be used in the most efficient manner.
[0065] The systems noted above can be combined and/or integrated
for the sharing and processing of data.
[0066] According to the invention, water content data is
categorized and/or associated with data detailing any notable
characteristics of the animals. All animals in any one grouping
have at least one characteristic that is shared between all
animals. For example, animals may be categorized according to an
age range, weight, sex, genetic composition and birthplace and the
measured water content data is compiled in a computer database. Any
number of categories can be established and the water content
measurement data of meat samples extracted from animals from the
same grouping can be collated so that it can be compared, combined
and/or used with other data acquired from other databases, such as
the GAM and EVT databases.
[0067] Measurement data acquired from animals can be transferred
and stored in the standards database so as to create a suitably
extensive database data that is representative of each category of
animal, enabling the determination of the naturally occurring water
content in meat that can then be used for the accurate control of
water content in meat.
[0068] The database created according to the invention can include
animal composition data detailing the elements and/or compounds
constituting any meat derived from the animal. The water content of
fat as distinct and separate from lean meat or muscle can also be
analyzed and the associated data for selected animals recorded in
the database accordingly. Data detailing the analysis of the
composition of lean meat or muscle for all animals in all
categories can also be recorded and such information used in any
manner, such as to control the water content.
[0069] RFID devices can be injected into an animal, or attached to
a tag to an animal extremity to identify an individual animal.
Another system utilizes an animal's eye retina to enable accurate
identification of an animal. Data associated with each animal can
then be recorded in a database.
[0070] In one embodiment of the present invention, an animal is
grouped into a category before slaughter, or immediately
thereafter, and assigned a water content standard representing the
natural water proportion of the meat or the fat. The animal can be
processed according to any method and at all times, any products
derived from the animal can be tracked to the animal, and the water
content throughout processing can be measured and adjusted to
within any percentage. For example, in one embodiment, the meat
flow rate is measured along with any water added to the meat, and
the water content of the meat is also measured. Typically, the meat
may have lost some water through evaporation or otherwise. The
added water may exceed the difference between the natural
proportion of water (as determined by the water content standard)
and the measured water content of the meat. Thus, to reduce the
water content of meat to its natural proportion, water can be
removed. The removed water is measured and metered to leave behind
that amount that will not cause the meat to have any water in
excess of the allowable. Thus, after processing, the meat contains
its natural proportion of water or any other desired amount. The
meat may be further measured after processing to ensure the water
content is within the desired amount. Alternatively, in other
embodiments, rather than achieving the natural proportion of water
in meat, the amount of water can be any amount allowed that can
also exceed the natural proportion. The meat can be packaged in a
low oxygen environment wherein the oxygen level is lower than air,
and the package can be provided with a label indicating the amount
of added water or the amount of water that is in the meat.
[0071] Referring now to FIG. 1, one embodiment of a method
according to the invention is schematically illustrated. The method
includes treating the goods with any suitable high pH agent that
can be a gas or liquid, such as sodium hydroxide solution,
potassium hydroxide solution, ammonium hydroxide solution, or
calcium hydroxide solution and that produces a high pH, as depicted
in block 102. The method is then followed by a secondary step
depicted by block 104, including exposure to a low pH agent that
can be a gas or liquid, such as a carbonic acid solution of carbon
dioxide and water in any selected, or relative quantities and at
any suitable pressure, and combined together in an effective manner
so as to produce carbonic acid of a suitably low pH.
[0072] The processes disclosed herein may be applied to any meat.
The processes can also be applied to paper pulp for bleaching
purposes and/or for killing any type of molds that may otherwise
survive the normal process of paper production or the production of
timber building products manufactured from wood chips. Any goods
may be processed with the apparatus and methods disclosed herein.
Representative examples of liquid and solid goods that can be
processed and/or decontaminated by the apparatus and methods
disclosed herein are listed below. Some solids may also be regarded
and processed in a manner that is suitable for liquids (such as
ground meats) and some liquids may be regarded and processed in a
manner that is also suitable for solids. Representative goods are
listed below under the headings of 1) "Substantially Liquids;" and
2) Substantially Solids":
[0073] 1) "Substantially Liquids" includes: meats; sausage; seeds
and grains; animal feeds; slurries; paper pulp used in production
of paper products (slurries); water for drinking; water (e.g.,
contaminated water); sewage.
[0074] 2) "Substantially Solids" include: salami, meats; hams;
frankfurters; poultry (whole, dressed and poultry pieces);
vegetables and fruits [hard and soft] (e.g., lettuce, cauliflower,
tomatoes, apples, melon, pears, oranges, broccoli); fish (whole sea
fish and freshwater, gutted or otherwise); beef primal portions
(e.g., strip loins, round, rump, tenderloin); timber or wood chip
raw materials used in building materials; waste food products
(e.g., waste from hotels, restaurants for recycling into animal
feeds).
[0075] The term GRAS refers to "Generally Regarded As Safe" and is
understood and used by the USDA, FDA, and those in industry to
describe substances that can be used with goods as additives.
Representative examples of GRAS substances are: sodium hydroxide,
sodium chloride, sodium chlorite, potassium chloride, and potassium
chlorite. These substances can be added in any form, before,
during, and after treatment with carbon dioxide and water according
to the invention.
[0076] The term "alkaline solution" includes a solution of an
alkali substance, such as ammonium hydroxide, sodium hydroxide,
potassium hydroxide, calcium hydroxide, tri-sodium phosphate, and
any other suitable alkali. These substances can be added in any
form, before, during, or after treatment with carbon dioxide.
[0077] The term "gas pressure" or "water pressure" refers to any
pressure that is suitable or effective for the particular
application, and may be controlled within any of the following
pressure ranges, or at any other suitable or effective
pressure:
[0078] gas at a pressure of about 0 psia to about 200 psia;
[0079] gas at a pressure of about 200 psia to about 500 psia;
or
[0080] gas at a pressure above about 500 psia.
[0081] water at a pressure of about 0 psia to about 200 psia;
[0082] water at a pressure of about 200 psia to about 500 psia;
or
[0083] water at a pressure above about 500 psia.
[0084] Representative approximated values of carbon dioxide
density, pressure, temperature and corresponding pH are shown in
the following table (Table 1):
1 TABLE 1 CO.sub.2 Density Pressure (PSIA) Temperature .degree. F.
pH -- 14.7 60 5.7 0.67 510 32 3.7 0.94 725 32 3.2 0.67 570 40 3.5
0.67 660 50 2.8 0.91 750 40 2.99 0.86 690 50 3.4
[0085] One embodiment of the present invention includes a method
for the treatment of goods, such as meat, with a high pH, alkaline
solution, followed by treatment with a low pH, acid solution,
wherein the acid can have a "temporary" low pH value. The pH of the
acid can be below about 7, including a pH of about 1 to about 3.
Optionally, the high pH alkaline solution or the low pH acid
solution can include a GRAS substance. The acid can have a
temporary low pH for the period of time during which it is being
used to decontaminate the meat. The pH of carbon dioxide and water,
for example, will increase when the pressure is reduced; thus, the
low pH level can be temporary. Water and carbon dioxide can be
mixed in any proportions, such as 3 moles of carbon dioxide mixed
with 2 moles of water. The pH of carbon dioxide and water is about
4 to about 5 when about 0.1 mol. (4.4 g) of carbon dioxide are
mixed with about 10 mol. of water (180 g), and about 2 to about 3
(pH) when about 20 mol. of carbon dioxide (88 g) are mixed with
about 10 mol. of water. However, in order to achieve these low pH
levels, the carbon dioxide should be capable of dissolving into the
water, which occurs at a pressure of about 750 psia at about 10
degrees centigrade, for example. Exposure of goods, such as meat,
to carbon dioxide and water, can be followed by exposure to
overwhelming quantities of liquid or dense carbon dioxide for the
purpose of decontamination. Table I shows the effects of
temperature and pressure on pH. In addition, low pH levels can be
achieved by adding compounds, such as sodium chlorite, sodium
chloride, and sodium hydroxide. Other substances can be naturally
occurring gases, that can evaporate when the process of
decontamination has been completed and the finished and processed
product is exposed to ambient atmospheric pressure. Alternatively,
naturally occurring liquid or solid processing agents, such as
water and/or salts, such as sodium chloride, can be used. Any
substances that will weaken pathogens and render them labile can be
used.
[0086] The use of high pressure carbon dioxide, enabling enhanced
solubility in water to create carbonic acid having a pH less than
about 3.0, can be regulated to effectively achieve the desired kill
rates while eliminating the potential deleterious effects of
retaining low pH acid in the goods. In one embodiment, lactate and
ethanol, in suitable quantities, are added to the goods intended
for processing, in combination with carbonic acid at high pressure.
After the process has been completed, the pH of carbonic acid can
be increased when the pressure is lowered to atmospheric pressure.
This provides a significant advantage when compared with the use of
acid that remains highly acidic at atmospheric pressure, such as
hydrochloric acid.
[0087] Additives such as sodium chlorite, ethanol, acetate,
citrate, and organic acid(s), such as citric acid, can also be used
by adding selected quantities, at the appropriate stage, which may
be applied in multiple, sequential stages, to achieve the desired
results.
[0088] The decontamination system according to one embodiment of
the invention can include a first high pH stage apparatus and a
second low pH stage apparatus. The low pH apparatus can use carbon
dioxide at a pressure above ambient pressure to produce carbonic
acid.
[0089] Referring now to FIG. 2, a schematic illustration of one
embodiment of an apparatus that can be used to treat goods, is
illustrated. The apparatus includes an inclined conduit portion
216. The inclined conduit portion 216 houses an internal screw
conveyor 236 that is driven by a variable speed motor 238. The
motor 238 drives screw conveyor 236 in the direction shown by arrow
212. The conduit 216 is arranged to transfer meat 202 along the
inside thereof and subsequently through a constriction portion 234
located at the end portion of the conduit 216. A fat measuring
device 218 (such as a Safeline-AVS x-ray device), is fitted to the
constriction portion 234. The upper end portion of conduit 216 is
open to allow passage of meat 202 into a container 222 located
beneath the opening.
[0090] A vertically disposed container section 206 is connected (at
the opposite lower portion of the conduit 216). The container
section 206 has an open end located directly under a conveyor 200.
The opposite lower end of container section 206 is open to the
inclined conduit 216 so as to allow the passage of meat from the
vertical container section 206 into the inclined conduit 216.
[0091] The continuous, horizontally disposed belt conveyor 200 is
arranged to carry the meat 202, directly from a carcass disassembly
room, for example. The conveyor 200 is arranged so that one end
will terminate above the opening of the container section 206. When
the conveyor belt 200 passes around the conveyor belt roller 204,
the meat 202 will drop downwardly and into the open end of the
vertically disposed container section 206.
[0092] The container section 206 includes an inlet port 228 for the
introduction of any suitable high pH alkaline solution. Any number
of spray nozzles 224 can be installed along the interior walls of
container section 206. Spray nozzles 224 can provide a spray 226 of
high pH solution thereby exposing the surfaces of the meat to the
high pH solution.
[0093] Alkaline solution can be maintained in the inclined section
216 and in the vertical container section 206 at any suitable
level, depicted by numbers 214 and 240, respectively, with the use
of any suitable level instrumentation. A drain (not shown) can be
located at any convenient location to drain solution from the
container 206 or inclined conduit 216. The variable speed drive
motor 238 can control the amount of exposure time of the meat to
the high pH solution by increasing or decreasing the speed of
rotation of screw 236. When the meat exits the constriction portion
234 of the inclined conduit section 216, the meat falls into the
storage container 222. From the storage container 222, the meat 232
can be transferred to any pressurized low pH stage apparatus
described below. Alternatively, the storage container 222 may be
omitted, in which case the meat exiting the apparatus can pass
directly into the low pH stage apparatus. In other embodiments,
there may be one or a plurality of operations before and after the
high pH and the low pH stage apparatus. These auxiliary unit
operations can perform various functions on the meat, such as
treating, decontaminating, irradiating, mixing, blending, grinding,
and the like.
[0094] Referring yet again to FIG. 2, the transfer screw 236 is
driven by motor 238, in such a way that pieces of meat are carried
through the conduit 216, after having been immersed in liquid 210,
wherein liquid 210 is a high pH alkaline solution, such as calcium
hydroxide or ammonium hydroxide solution. Portions of meat 202 are
transferred through the liquid 210, and ejected from the end of
conduit 216 through constriction 234. The constriction 234 can
ensure that the meat portions are compressed prior to passing
through fat measuring device 218. The fat, water, and lean meat
content of the meat portions can be measured prior to depositing in
container 222.
[0095] Referring now to FIG. 3, one embodiment of an apparatus for
decontaminating goods is illustrated. The apparatus can use any gas
or blend of gases, which can also include the addition of any salt
or solution thereof or any suitable substance in measured
quantities, at any suitable pressure and temperature. In one
embodiment of the apparatus, the apparatus can be used as a low pH
stage apparatus, that follows the high pH stage apparatus, such as
the one illustrated in FIG. 2. In one embodiment, carbon monoxide
may also be added. In yet another embodiment, organic acids, such
as anti-oxidants, including citric acid, may also be added in
solution. The pH within the apparatus can be varied according to
the pressure of the carbon dioxide contained therein.
[0096] Referring still to FIG. 3, the apparatus includes a first
processing vessel 312 having an entry port 366 for the goods 308,
such as meat, and an entry port 358 for carbon dioxide and water
300. The vessel 312 can be operated at any pressure ranging from
about 500 psia to about 800 psia. The vessel 312 includes a
transfer screw (not shown) to transfer the goods from one end of
the vessel to the opposite end of the vessel 312. In one
embodiment, this screw can have paddles, or other means, to cause
the boneless meat to blend and mix with the carbonic acid produced
from carbon dioxide and water. The screw can operate at a speed
which will provide adequate retention time within the vessel to
kill microorganisms, including pathogens or bacteria, that reside
on the meat. The vessel 312 can include a narrowing section 320
that leads to a conduit 336 of reduced diameter. The conduit 336
can have one or more grinding heads 310. The conduit 336 can open
into a second vessel 322 through valve 310. The second vessel 322
can be operated at a reduced pressure as compared with the first
vessel 312. The second vessel 322 can be operated at a pressure
from about ambient (about 14.7 psia) to slightly below the pressure
of vessel 312. The vessel 322 can have a conduit 302 located at an
upper portion of vessel 322 for any gas or moisture to exit the
second vessel 322. The vessel 322 can also have a conduit 306 for
meat to leave vessel 322.
[0097] In one embodiment, liquid carbon dioxide and liquid water
are injected into port 358 at a pressure from about 200 psia to
about 500 psia. The amount of liquid and carbon dioxide can be
measured. Water can also be measured and introduced along with the
carbon dioxide. Alternatively, the carbon dioxide and the water can
be introduced at two distinct and separate injection ports. The
amount of carbon dioxide can be based on the desired pH in vessel
312 or based on the pressure desired in vessel 312 or based on the
quantity of water. Water can be any percent, such as 2%, of the
mass flow rate of meat, plus any additional moisture that may be
lost through evaporation. The water can additionally include salts,
such as sodium chloride or sodium chlorite.
[0098] Carbon dioxide can be vented as a result of the drop in
pressure in vessel 322. Carbon dioxide vents through port 302. The
vented carbon dioxide may carry moisture. The decontaminated meat
can be transferred out of the vessel 322 through port 306 and
further processed in any desired manner.
[0099] In another embodiment, a rotating screw can be provided at
the exit of vessel 312, at the union of the high pressure vessel
312 with the low pressure vessel 322. The rotating screw can be
arranged to allow for decompression, and pressure reduction,
gradually. To this end, the rotating screw can have gradually
increasing volume between the flights of the screw.
[0100] Continuing to refer to FIG. 3, the narrowing section 320 of
vessel 312 can have perforations. An annular space 330 can be
provided between the perforated section and the exterior wall of
vessel 312. Ports 346 and 348 leading from the annular space 330
are arranged to allow gases and liquids to be extracted therefrom.
The gases and liquids can then be recycled after conditioning in
vessel 360, where the liquids may be removed from the gas. The gas
is compressed by compressor 368. Compressed gas can be transferred
via conduit 354 and recycled by injection into vessel 312 through
port 362. Meat can be transferred along conduit 271. Recycled
carbon dioxide gas from conduit 354 can be combined with water and
injected into port 362. The quantity of water added can be directly
proportional to the quantity of meat processed. The water can be
about equal to the amount of moisture loss that has occurred or
will occur during processing. The quantity of water added may also
be controlled to not exceed any legally allowed amount as directed
by the United States Department of Agriculture (USDA) or any other
such responsible federal or state government body of any country.
After compression and grinding of the meat in conduit 350, the meat
then passes into conduit section 352. The pressure at conduit
section 352 can be about 50 psia less than the pressure at
perforated section 320. Port 319 is provided to inject goods, such
as LFTB. The meat, that may include LFTB, can be transferred into
vessel 322 after passing through valve 318. The pressure at
perforated section 320 is affected by the rate of flow through
grinders 310 and the pressure at conduit 352 can be controlled by
the opening and closing of the valve 318. Valve plug 334 can mate
with valve 318 so as to close conduit section 352. Valve plug 334
is rigidly attached to rod 330 such that an opening and closing
force can thereby be applied to rod 330. The opening and closing
force applied to rod 330 is sufficient to open and close the valve
thereby preventing any goods from passing through or allowing the
passage and the drop in pressure. Screw 324 in vessel 322 is
arranged to transfer the meat away from vessel 322.
[0101] Meat is introduced into the high pressure vessel 312 through
the injection port 360 by a variable speed pump (not shown). The
meat is pumped at a pressure which can range from about 200 psia to
about 850 psia. Instruments to measure level, flow, pressure, and
temperature are located on all the appropriate conduits and
vessels. In this manner, the amount of liquid or gaseous carbon
dioxide and/or alternatively, the amount of water, can be
controlled at a measured quantity based on the measured quantity of
meat. The meat can be transferred in a continuous rate which may be
adjusted as required by the variable speed pump, and the amount of
carbon dioxide and water can be adjusted continuously and at a rate
that corresponds and/or is proportionally related to the rate of
the meat.
[0102] The retention time within the processing vessel 312 can be
adjusted by the variable speed motor that drives the transfer screw
within vessel 312 to ensure that the desirable number of
microorganisms are destroyed. This number may exceed 5 log. The
process can be capable of destroying at least a number of
microorganisms equal to 10 to the log 5 (10.sup.5). The process can
also meet HACCP minimum standards.
[0103] Carbonic acid is the acid that is generated by the
combination of carbon dioxide and water. However, under standard
temperature and pressure conditions, the resultant acidic solution
is only mildly acidic, having a pH of about 6. In one embodiment,
the pressure in the high pressure vessel 312 can be about 500 psia
and the temperature can be about 0.degree. C. At this temperature
and pressure, the pH of the liquid is about 3 to about 4. The pH
can be controlled by adjusting the pressure in the high pressure
vessel 312. For example, pressure can range from about 200 psia to
about 850 psia, or greater than 850 psia.
[0104] The carbon dioxide can decontaminate and chill the meat and
then evaporate leaving no residue other than water in vessel
322.
[0105] Referring now to FIG. 4, a cross section through one
embodiment of an apparatus that can be used for decontaminating
goods, such as meat, and lean fine textured beef (LFTB), is shown.
The apparatus may be used as the low pH stage apparatus, following
a high pH stage apparatus. Meat, such as LFTB, can be loaded into a
vessel, and water can be blended with the LFTB so that the combined
water and LFTB have a texture of a paste that can be pumped. The
paste is then transferred along conduit 412. The apparatus of FIG.
4 comprises an injection pump 410, and an extraction pump 426, and
a pressure vessel 400, interposed between pumps 410 and 426, and
connecting them together via conduits 440 and 438. Each pump has a
set of pistons. Pistons 406 and 408 of injection pump 410 operate
in concert with valve 404, held within housing 442. The twin
cylinders and valve that comprise injection pump 410, can be
supplied by Marlen Research Corporation. Pistons 406 and 408
reciprocate alternately, extracting LFTB paste from a vessel and
compressing the LFTB to a selected pressure, such as about 850
psia, and injecting the LFTB via valve 404 into conduit 440. The
LFTB can be pumped at a selected mass flow. Extraction pump 426
operates similarly to injection pump 410, to extract LFTB from
pressure vessel 400, at a rate about equal to the rate of
injection. Extraction pump 426 also comprises two pistons, 422 and
424, with valve 428, held within housing 444. Extraction pump 426
extracts LFTB from conduit 438, and transfers the LFTB into conduit
436. The LFTB can be transferred into any vessel via conduit
436.
[0106] Referring again to FIG. 4, port 418 is connected directly to
a source of carbon dioxide that may be liquid or gas, and can be at
a pressure greater than about 850 psia. Carbon dioxide can be
transferred via port 418 to contact the LFTB within vessel 400. The
carbon dioxide transferred into vessel 400, blends with the LFTB
and water also injected into vessel 400 by injection pump 410. The
mass flow rate of LFTB and carbon dioxide can be controlled in
direct proportion to each other at selected mass flow rates. The
carbon dioxide gas blends with LFTB and water, thereby producing
carbonic acid. The flow rates provided by injection pump 410,
extraction pump 426, and the carbon dioxide gas supply via port
418, are arranged so as to make sure that the pressure within
pressure vessel 400, is maintained at about 850 psia. At this
pressure, the pH of the carbonic acid and water that blends with
the LFTB inside pressure vessel 400 can be about 2 to about 3.
Bacteria that may be present with the LFTB upon injection into
pressure vessel 400 can be in direct contact with the highly acidic
carbonic acid also contained within pressure vessel 400. The
process can be controlled such that the retention time of the LFTB
with water and carbon dioxide (carbonic acid), is sufficient to
ensure that substantially any bacteria that is present on the LFTB,
is killed. After processing, the decontaminated LFTB transferred by
extraction pump 426, into conduit 436, can be blended with other
ingredients thus avoiding cross contamination of the other
ingredients.
[0107] Referring now to FIG. 5, one embodiment of a low pressure
vessel 504 is shown. Vessel 504 is similar in operation to vessel
322 of FIG. 3, and may be substituted therewith. Vessel 504 has
conduit 502 on the upper side of vessel 504 to allow venting of
gases. These gases may be exhausted directly to atmosphere, or
alternately processed before venting. Conduit 508 can be attached
to a source of decontaminated meat. Meat, such as ground beef, can
be transferred into vessel 504, via port 508. Port 510 may be
connected to a source of decontaminated LFTB, such as may have been
processed with the apparatus described in association with FIG. 4.
The rate of mass flow of LFTB transferred via conduit 510 is
related to the rate of mass flow of meat transferred via conduit
508. Meat injected via conduit 508, and LFTB injected via conduit
510, can blend together as a consequence of agitation caused by the
screw 514, and the expansion of the carbon dioxide gas carried with
the LFTB. Liquid or gas carbon dioxide can be further injected via
ports 516 and 518 that can impinge on screw 514. The carbon dioxide
gas will cause cooling of the meat and LFTB as it expands in vessel
504, prior to exhausting via conduit 502. The chilled and blended
meat and LFTB is then carried from vessel 504, via conduit 528 by
transfer screw 514. Conduit 528 can be directly connected to other
processing or packaging equipment so as to enable further
processing or packaging of the meat and LFTB.
[0108] Referring now to FIG. 6, an apparatus that can be used to
continuously decontaminate goods, such as meat, is illustrated. The
apparatus can be used as the low pH stage apparatus, following a
high pH stage apparatus. A series of three cylinders with pistons
are arranged radially around a central point. Cylinders 610, 612,
and 614, are arranged with internally mounted pistons 626, 622 and
624, respectively therein. Hydraulic cylinders 616, 618, and 620
are connected via connecting rods to pistons 626, 622, and 624,
respectively, such that pistons can reciprocate forwards and
backwards as shown by arrows 642, 644, and 630. Inlet conduits 638,
634, and 636, arranged perpendicular to cylinders 610, 612, and
614, respectively, can carry meat into the cylinders. Valves 628,
632, and 630 are arranged at the opposite end of the inlets 638,
634 and 636, to both allow and prevent the flow of meat from within
the corresponding cylinders during the reciprocating cycles.
[0109] With reference to the cylinder 614 with piston 624, meat can
be injected via conduit 636. Meat can be pumped until cylinder 614
is filled, and piston 624 is fully retracted in hydraulic cylinder
620. Valve 630 is closed during filling. With respect to cylinder
610, and piston 626, meat has already filled cylinder 610. However,
valve 628 remains closed. Piston 626 is in the fully retracted
position. Cylinder 612 with piston 622 has valve 632 in an open
condition allowing meat that has been processed with carbonic acid
at high pressure and retained for an effective period of time, to
be transferred out of cylinder 612 by movement of piston 622. The
three cylinder and piston assemblies can be operated sequentially
wherein one cylinder can be filled with meat, one cylinder can be
in the process of being filled, and one cylinder can be in the
process of being emptied.
[0110] Referring now to FIG. 7, an apparatus that can be used to
decontaminate goods, such as meat, is illustrated. The apparatus
can be used as the low pH stage apparatus, following a high pH
stage apparatus. A vertically disposed pressure vessel 700 is
arranged with ports. A centrally and vertically disposed stirring
mechanism 740 is attached to a variable drive motor 752 such that
stirring mechanism 740 rotates slowly in the direction shown by
arrow 712. Conduit 742 is at the exit end of vessel 700. A grinding
plate 730 is mounted in conduit 742 with space 744 on the upstream
side of grinding plate 730 and space 738 on the downstream side of
grinding plate 730. Conduit 742 can connect vessel 700 with an
expansion vessel 736. Conduit 734 empties into space 738 so that
goods, such as meat or LFTB, can be pumped into conduit 742. Port
708 on vessel 700 allows the transfer of meat under high pressure,
such as about 850 psia. Conduit 702 is arranged to allow the
injection of carbon dioxide and water into vessel 700. A compressor
718 is connected to an inlet conduit 716, which discharges to an
outlet conduit 724. A pressure release conduit 720 is also
provided. Pressure release conduit 720 is fitted with a pressure
release valve 722, which allows the escape of gas when the pressure
exceeds a pre-selected pressure. Carbon dioxide gas compressor 718
extracts carbon dioxide gas via port 750 from inside the vessel
700. After compression of the carbon dioxide gas by compressor 718,
the compressed gas is then re-circulated into pressure vessel 700,
via conduit 724 through ports 726 and 728 at the base of the
vertically disposed pressure vessel 700 at a selected mass flow
rate. Meat is injected into the pressure vessel 700 via conduit 708
at a selected mass flow rate. Carbon dioxide and water is injected
via port 702 into vessel 700 at a selected mass flow rate. The meat
will be exposed to and blend with the water and carbon dioxide. The
meat can fill vessel 700 to a pre-selected level before grinder
plate 730 commences grinding. In this way, the meat will be
retained within pressure vessel 730, for an effective time period
which will expose the meat to carbonic acid and kill bacteria. The
vessel 700 operates at high pressure, such as about 850 psia.
Carbon dioxide gas at a pressure of about 850 psia is lighter than
the meat and water contained within vessel 700. At this pressure,
the density of carbon dioxide will be about 0.8 g/cc which is less
than the density of meat and water, and will therefore tend to
accumulate at the upper end of the vertically disposed pressure
vessel 700. Port 750 is so located and arranged to allow extraction
of the carbon dioxide gas via conduit 716. Compressor 718 will
elevate the pressure of carbon dioxide by about 25 to about 50 psi,
and then recycle the compressed gas via conduit 724, through ports
726 and 728. The dense carbon dioxide gas will flow upwardly and
blend with the meat, that is agitated by agitator 740, and in doing
so, will ensure that water contained within vessel 700 is saturated
with carbon dioxide, forming highly acidic carbonic acid. The
carbonic acid will destroy pathogens that may be present at the
surface of the meat. After an effective period, such as about 10
minutes, the meat can be extracted from the pressure vessel 700 via
conduit 742, through grinder 730 that will be arranged to grind at
a selected rate about equal to the rate of meat injection via
conduit 708. If so desired, LFTB, having been processed according
to the process described in association with FIG. 4, can be
injected via port 734. Pressure and temperature within pressure
vessel 700 can be adjusted to provide the pH effective to kill
microorganisms, such as bacteria.
[0111] Referring now to FIG. 8, an apparatus for processing and
decontaminating goods, including meat, is shown. The apparatus
shown in FIG. 8 resembles the apparatus described in association
with FIG. 7, however some additional components have been provided
as described below. Conduit 866 with valve 858 is shown connected
to the upper end of pressure vessel 800. Conduit 866 can
automatically and suddenly allow the injection of any liquid or
gas, such as high pressure carbon dioxide gas or liquid, into
vessel 800 by operation of valve 858. Conduits 808 and 802 are
shown with valves 860 and 862, respectively. Also, conduits 826 and
828 are shown with valves 868 and 870, respectively, and conduit
816 is shown with valve 876. Additionally, conduit 834 is shown
with valve 872, and conduit 842 has a gate valve 874, wherein valve
874 is interposed between grinder 830 and vessel 800. The purpose
of the valves is to isolate vessel 800 to allow the retention of
meat under pressure. The arrangement of valves as shown in FIG. 8
allows meat, carbon dioxide, and water, to be transferred into
vessel 800 and held under high pressure for an effective period.
Water and carbon dioxide can be added to vessel 800 via conduit
802. Meat can be added to vessel 800 via conduit 808. At this time,
the pressure inside vessel 800 is about 500 psia. Carbon dioxide
gas transferred through conduit 866 will be at such pressure so as
to elevate the pressure within vessel 800, to a pressure of about
850 psia to about 1000 psia. By so doing, the pH of the carbon
dioxide and water (carbonic acid), will decrease in a short amount
of time to a pH less than about 3. The increase in pressure can be
produced suddenly by opening valve 858 to cause a sudden and
substantial pH reduction. Pathogens, such as E. coli 0157:H7, can
be killed rapidly by "shocking" the organisms in this manner (i.e.,
the sudden and substantial lowering of the pH of an acidic
solution, with which the organisms are in contact). Such a
condition can cause death of these pathogens within a few seconds.
Other pathogens, such as salmonella, can also be killed in this
manner.
[0112] Referring now to FIG. 9, an embodiment of a valve is shown.
Annular valve plug 914 is rigidly attached to a shaft 902 and is
arranged so as to reciprocate up and down in the directions shown
by arrow 904, by a powered driver, such as a hydraulic cylinder
capable of providing opening and closing forces. Conduit 906
terminates in a bell-shaped opening with an annular internal
surface valve seat 922, that mates with annular external surface
920 of valve plug 914. Valve plug 914 can be positioned in either
the fully open position (shown in solid line), or the fully closed
position (shown in dashed lines 910), wherein annular surface 920
of valve plug 914 is in direct contact with internal annular
surface of valve seat 922. When valve plug 914 is in the open
position, meat can exit conduit 902. The valve described in
association with FIG. 9 is similar to valve 318 shown in
association with FIG. 3.
[0113] Referring now to FIGS. 10 and 11, an apparatus for
continuously processing and decontaminating goods, such as meat, is
shown. A horizontally disposed conduit 1002 is mounted to a frame
1000 that is rigidly fixed to concrete or other suitable flooring.
A series of conduits fitted with valves are provided along the
upper section of conduit 1002 so as to allow direct passage to the
interior of conduit 1002. Hydraulic cylinders 1042 and 1048 are
rigidly mounted to backing plate frames 1046 and 1052 on opposite
ends of the conduit 1002, respectively. Pads 1044 and 1050 are
attached via piston rods to the hydraulic cylinders 1042 and 1048,
respectively. The hydraulic cylinders are arranged in line with
conduit 1002 and on opposite ends thereof, in such a manner, that a
compressive force can be applied between pads 1044 and 1050. Cages
1028 are located within conduit 1002 and between pads 1044 and
1050. Each cage 1028 comprises two end plates connected by bars,
that will be more clearly described below in association with FIGS.
12-16. Each end of a cage comprises a piston that fits in an
airtight manner within the bore of conduit 1002. The cages can be
transferred through conduit 1002. The cages are placed end to end,
so as to make contact with each other and are held under
compression between pads 1044 and 1050. Conduit 1002 allows at
least one cage to be completely outside of conduit 1002 at either
end for insertion and removal. Baskets 1036 can be filled with
goods and then located and held within the cages. Baskets can be
manufactured from an open mesh material with an opening along one
side and a hinged door that can be closed to cover the opening in
such a manner so as to retain goods therein. Baskets can be placed
inside cages and transferred with the cages along the inside of
conduit 1002. The pistons of cages comprise seals that are arranged
in such a way that the seals intimately contact the inner surface
of conduit 1002. In operation, the oil pressure in hydraulic
cylinder 1042 can be elevated to a pressure above the pressure that
is within hydraulic cylinder 1048 and allows pad 1044 to move in
the direction of arrow 1058 and causes the cages similarly to move
in the same direction. Clamp 1040 can be mounted to the inlet end
of conduit 1002 and clamp 1038 can be mounted to the exit end of
conduit 1002. Clamps 1040 and 1038 can be operated by powered means
so as to clamp between two adjacent cages, and in doing so prevents
any lateral movement of the cages, when desired. Hydraulic
cylinders 1042 and 1048 can be withdrawn completely, allowing the
removal of one cage in contact with pad 1050, at the exit of
conduit 1002 and the relocation of another cage at the entrance to
conduit 1002. A loaded basket is placed in a cage to be located at
the entry end to conduit 1002, and pistons 1042 and 1048 are again
extended so as to compress the cages together. At this time, clamps
1040 and 1038 are withdrawn, allowing hydraulic cylinder 1042 to be
operated by higher pressure than hydraulic cylinder 1048, thereby
transferring the assembly of cages. This indexing process is
repeated sequentially and each time a cage with basket is removed,
a cage loaded with a basket, is placed at the entry to the conduit
1002 on the guide 1030. In this way, cages with baskets containing
goods are progressively indexed along the bore of conduit 1002 for
processing. A series of conduits 1006 with valves 1008 allow the
injection of water and carbon dioxide into conduit 1002. Carbon
dioxide and water can be injected via conduits 1006 at a pressure
of about 500 psia, while conduits 1012 and valves 1013 can be
arranged to inject water and carbon dioxide at a pressure of about
1000 psia. Conduit 1016 and valves 1014 can be arranged to allow
the exhausting of lower pressure carbon dioxide and water, and
conduit 1020 with valves 1018 can be arranged to exhaust the higher
pressure carbon dioxide and water. In this manner, the goods in
each cage can be exposed to a series of relative low and high pH
mixtures of carbon dioxide and water. Carbon dioxide and water from
conduits 1006 at low pressure can be allowed to pass into the
sections of conduit 1002 isolated between the two ends of a cage,
and then exhaust through conduit 1016 when valve 1014 is open.
Valves 1014 and 1018 can then be closed, and after transfer of
cages in the direction shown by arrow 1058, higher pressure carbon
dioxide and water from conduits 1012 can be transferred into the
space isolated by the two ends of the same cage and then exhaust
through conduit 1020 when valve 1018 is open. As cages with baskets
and goods therein are transferred along conduit 1002, a series of
low pressure treatments followed by high pressure treatments, can
be provided, thereby exposing goods in baskets to varying levels of
pH, in a rapid and "shocking" manner. By alternately exposing goods
to low and high pressure, with corresponding high and low pH,
pathogens and undesirable bacteria that may be present on the
surface of goods contained in baskets, can be killed. Immediately
prior to the transfer of any cage, out of conduit 1002 and onto
support section 1032, valve 1068 in conduit 1066 can be opened to
allow any gas contained in the cage to equilibrate with atmospheric
pressure prior to transfer out of conduit 1002. FIG. 11 shows a
cross section through conduit 1002 and injection ports.
[0114] Referring now to FIGS. 12, 13, 14, 15, and 16, various end
and cross sectional views are shown of a representative cage 1028
as disclosed for use in association with the apparatus of FIG. 10.
End piece 1108 and end piece 1116 are connected by rods 1100. End
pieces 1108 and 1116 are circular as shown in the respective end
views. Seals 1104 and 1102, and seals 1110 and 1112 are fitted to
end pieces 1108 and 1116, respectively. End pieces 1108 and 1116
are arranged to fit snugly, like pistons, such that seals will
firmly contact the internal surface 1032 of conduit 1002 shown in
FIG. 11. In this way, the assembled cage as shown in FIG. 12, can
be transferred along conduit 1002, to withstand respective high and
low pressure mixtures of carbon dioxide and water, whereby seals
1104, 1102, 1110, and 1112 contact surface 1032 in a pressure-tight
manner.
[0115] Referring now to FIG. 14, a slot 1106 is profiled in the end
piece 1108 so as to mate with a ridge 1114 of an adjacent end piece
1116, as shown in FIG. 16, when the respective end pieces 1108 and
1116 are located in conduit 1002. In this manner, cages can be held
interlocked together such that when drive shaft 1062 is rotated by
drive motor 1060, the interlocked cages, will rotate. Goods in
baskets located in cages, can be rotated so that the outer surfaces
of any goods contained in the baskets will be exposed to the carbon
dioxide gas and water used in the process.
[0116] Referring now to FIGS. 17, 18, 19, 20, 21 and 22, cages are
shown with end pieces 1218 and 1220 connected by rods 1200, that
allow for interlocking adjacent cages. Seals 1204 and 1202 are
fitted to end piece 1218, and seals 1208 and 1210 are fitted to end
piece 1220. End piece 1218, as shown in FIGS. 18 and 19, is
arranged with a slot 1206, that can mate with a corresponding tab
1212 of end piece 1220 as shown in FIG. 21, so that interlocking
between adjacent cages takes place as can be seen in FIG. 22. This
configuration allows rigid coupling of adjacent cages. It should be
noted that when cages are either removed from the exit end of
conduit 1002 shown in FIG. 10, or loaded at the entry end of
conduit 1002 in FIG. 10, slot 1206 and tab 1212 are aligned so as
to allow for connection or disconnection. This can be achieved by
the correct positioning by drive motor 1060, and monitoring the
actual location of cages, which can be indicated by a proximity
strip 1026 running the full length of conduit 1002. Proximity strip
1026 is arranged in direct external contact with conduit 1002 in
such a way that will allow the detection of the precise positioning
of the end pieces of each cage so as to position cages at the
respective high and low pressure stations. Additionally, RFID tags
may be located and attached to each cage, thereby providing a way
of detecting the location of each cage and basket.
[0117] Referring now to FIG. 23, a cross sectional view through an
embodiment of an apparatus that can be used to decontaminate goods,
including meat, is shown. The apparatus shown in FIG. 23 combines
some of the previously described vessels. For example, vessel 1354
can operate similarly to the vessel 800 described in association
with FIG. 8. Vessels 1308 and 1302 can operate similar to vessels
330 and 322 of FIG. 3, and vessel 504 of FIG. 5. The apparatus is
arranged to decontaminate goods in a multiple stage process.
Conditions can be provided in the vessels so that the goods can be
exposed to a first treatment, in a first vessel, and then to a
second treatment, in a second vessel, that can be similar or
different to the first treatment. If so desired, a third treatment
may be provided in a third vessel and so on. The vertically
disposed pressure vessel 1354 is arranged with a series of ports
that communicate directly with the inside of vessel 1354. A
centrally and vertically disposed stirring mechanism 1412 is
attached to drive motor 1424 such that the stirring mechanism 1412
can be rotated in direction of arrow 1366. Meat can be introduced
into the vessel 1354 through the conduit 1362 by a pumping
apparatus (not shown), such as a Marlen Pump of Marlen Research
Corporation, of Overland Park, Kans., USA. The meat is pumped at a
pressure which can range anywhere from about 200 psia to about 600
psia, or greater. Mass flow control valves, flow measurement,
pressure, temperature or other instruments are located on the
appropriate conduits to measure and control meat, carbon dioxide,
and water going into vessel 1354. In this manner, the amount of
liquid or gaseous carbon dioxide and/or alternatively, the amount
of water and selected additives can be controlled at a measured
quantity based on the measured quantity of meat. A constant ratio
of meat, carbon dioxide gas (or liquid), and water can be
transferred into vessel 1354 at a selected and continuous combined
rate of mass flow.
[0118] Conduit 1414 connects vessel 1354 with vessel 1408. A
grinding plate 1402 can be mounted in conduit 1414. Alternatively,
the grinding plate can be omitted. A conduit 1406 is connected to
conduit 1414 so that goods, such as LFTB, can be introduced. Vessel
1408 is connected to conduit 1308. An insulated screw 1454 is
mounted within conduit 1308 to transfer goods through conduit 1308,
and which can also elevate the pressure to about 1050 psia. The
vessel 1308 can be operated at a pressure from about 500 psia to
about 1050 psia. The transfer screw 1454 can additionally be
configured to induce mixing of the goods and can be attached to an
electrical power source 1442. The transfer screw 1454 can be
arranged with insulation 1438 so that power source 1442 can be
attached to a collar 1444 in such a way that electrical current
will flow through the transfer screw 1454 which is in direct
contact with goods. In this way, an electrical current of variable
and selected voltage can be passed through the goods, as the goods
are transferred through conduit 1308. The vessel 1308 includes a
gradually narrowing perforated section 1318 that leads to a conduit
1334 having a reduced diameter. Conduit 1334 can have one or more
grinding heads 1306 provided therein. The conduit 1334 opens into
the vessel 1302 via valve 1314. The perforated section 1318 is
located downstream of transfer screw 1454, so that goods being
transferred are compressed while passing through the perforated
section 1318. The perforated section 1318 is surrounded by annular
spaces 1328 and 1456 enclosed within conduit's 1308 exterior walls,
which in turn are connected to conduits 1344 and 1346. Conduits
1344 and 1346 leading from the annular spaces are arranged to allow
gases and liquids to be extracted from the meat, prior to grinding.
These extracted gases and liquids can be subsequently recycled
after conditioning in vessel 1432, where liquids may be removed
from the gas via conduit 1340. The gas can be compressed to a
suitable pressure by compressor 1436. Gas compressed by compressor
1436 can be transferred via conduit 1352 and can be recycled by
injection into either of vessels 1354 and 1308 at ports 1462 and
1460, respectively, or at any other suitable port. Meat that is
transferred along conduit 1308 can be compressed before grinding
and then transferred along conduit section 1350 after grinding. The
pressure at conduit section 1350 can be about 50 psi less than the
pressure at conduit section 1334. An inlet port 1316 is provided
along conduit section 1350, so as to allow the injection of goods,
such as LFTB (Lean Fine Textured Beef) therein, at a suitable and
controlled rate. The meat, which may include LFTB, is transferred
into vessel 1302 after passing through valve 1314 and around valve
plug 1332. The pressure in conduit 1334 at the location immediately
upstream of grinders 1306 is affected by the rate of flow through
grinders 1306. The pressure at section 1350 immediately downstream
of grinders 1306, is controlled by the valve 1314. Valve 1314 can
enable the complete closing at the exit end of conduit 1350. Valve
1314 is rigidly attached to rod 1328 that can provide opening and
closing forces. The opening and closing force applied to rod 1328
is sufficient to completely close the valve thereby preventing any
goods from passing through. In this way, the pressure drop that
occurs when the goods are transferred into vessel 1302 will occur
at the end of conduit 1350 immediately prior to transfer through
the valve 1314, thereby allowing any chilling or freezing caused by
the rapid decompression of carbon dioxide to occur at the point of
exit. Screw 1322 mounted in the lower interior section of vessel
1302, is arranged to extract meat from vessel 1302. Recycled gas
from compressor 1436 can be transferred for repeated use by
combining with water and other selected substances, and injected
into vessel 1408 via port 1460. The water added to the meat can be
directly proportional to the quantity of meat. The amount of water
can include the moisture loss that will occur as a result of
processing the meat, after harvesting from the animal, and prior to
packaging. The quantity of water added may also be controlled so as
not to exceed any allowed amount, such as directed by the USDA (in
the USA) or any other responsible Federal or State Government
body.
[0119] The vessel 1302 is operated at a lower pressure as compared
with the vessel 1308. The vessel 1302 is operated at a pressure
from about ambient pressure or about 14.7 psia to about 20 psia or
alternatively the pressure can be any pressure that is lower than
the pressure in vessel 1308. The vessel 1302 has a conduit 1300,
located at an upper location to exhaust any evolved gas or
entrained moisture, from vessel 1302.
[0120] Liquid or gas carbon dioxide, and water at a pressure from
about 200 psia to about 500 psia can be injected into vessel 1354
through port 1356. Carbon dioxide and water can be measured. The
amount of carbon dioxide can be based on the pH desired in the
vessel, or on the pressure desired so as to induce such desired pH,
or based on the quantity of water or meat. The water can include
the water that is anticipated will be lost through evaporation or
otherwise. The vessel 1308 receives the liquid carbon dioxide, the
liquid water, and the meat from vessel 1354 and 1408. Sodium
chloride solution or any other suitable substance can be provided
in vessel 1408 via conduit 1446, and in such quantities that will
assist in lowering the pH of the carbon dioxide and water to about
1 to about 2. Screw 1454 causes the goods to blend and mix with the
carbon dioxide, water and salt solution at a pressure of about 1050
psia. The goods are carried forward and at a speed that will
provide adequate retention time within the vessel 1308 to ensure
adequate killing of microorganisms, including pathogens or bacteria
that reside on the goods. The sodium chloride or other salt
compounds can be washed with water or other suitable washing agent
after processing.
[0121] The goods can be ground by grinders 106. One embodiment of
the apparatus includes one or more meat grinders 1306 disposed
between vessel 1308 and vessel 1302. If more than one grinder is
used, a coarse grinder can be followed by a fine grinder.
[0122] Following grinding, the contents of the vessel 1308,
including meat, carbon dioxide, water, and salt, are emptied into
the vessel 1302, that operates at a lower pressure relative to
vessel 1308. The pressure in vessel 1302 can range from about
atmospheric pressure (14.7 psia) to slightly below the pressure of
vessel 1308. Carbon dioxide is vented through port 1300 from the
vessel 1302. The vented carbon dioxide may carry moisture that can
be compensated for with the addition of water. The meat can be
transferred out of the vessel 1302 and further processed in any
desired manner.
[0123] In another embodiment, a screw can be provided in conduit
1334 that allows for the gradual depressurization by increasing
volume as meat travels down the screw.
[0124] The pressure and temperature in vessel 1354 are about 500
psia and about 10.degree. C. At this temperature and pressure, the
pH is about 3 to about 4. The pH can kill microorganisms, including
bacteria and pathogens, and can also cause acid resistant
organisms, such as some strains of E. coli 0157:H7, to be weakened
in the normal homeostasis process. After an effective residence
period in vessel 1354, the meat can be transferred via conduit 1414
and vessel 1408 into vessel 1308. Sodium chloride or sodium
chlorite solution added to the carbonic acid solution can cause the
lowering of the pH in conduit 1308 to about 1 to about 2. Organisms
that have been subjected to the conditions in vessel 1354 are then
exposed to a lower pH in vessel 1308. Under these conditions,
organisms that may have survived the energy exhausting conditions
in vessel 1354 will not be able to survive the higher acidic
conditions in vessel 1308. The pH can be controlled by adjusting
the pressure of the vessels 1354 and 1308 and adding other pH
adjusting substances. For example, some embodiments can use a
pressure as low as about 200 psia, alternatively, some embodiments
may use a pressure of greater than about 500 psia or some
embodiments can use any pressure ranging from about 200 psia to
about 1050 psia. Additionally, by passing an electrical current
through the goods in conduit 1308, the organisms will be subjected
to conditions that will inhibit their capability to maintain an
internal pH.
[0125] One advantage of the methods described herein is that carbon
dioxide can be used both to decontaminate and chill the meat, and
afterwards, the carbon dioxide can evaporate leaving no residue
other than water and in some cases a small amount of residual salt.
The water added that is injected into the vessels 1354 and 1308 can
be calculated and controlled, so that at the end of processing, the
meat will have an allowable amount of water that can be the natural
proportion of water, as determined by the standards or
otherwise.
[0126] Conduit 1362 of vessel 1354 allows the transfer of meat
under high pressure, such as about 500 psia. Conduit 1356 is
arranged to allow the injection of carbon dioxide and water. A
compressor 1390 is connected to an inlet conduit 1370, an outlet
conduit 1396 and a pressure release conduit 1392. The pressure
release conduit 1392 is fitted with a pressure release valve 1394,
which allows the escape of gas when the gas exceeds a pre-selected
pressure set point that will cause venting of gas. Alternatively,
carbon dioxide gas can be recycled after release into conduit 1392.
Carbon dioxide gas compressor 1392 extracts carbon dioxide gas via
port 1422 from vessel 1354. After compression, the carbon dioxide
gas is then re-circulated into vessel 1354, via conduit 1396
through ports 1400, and 1398 at the base of the vertically disposed
vessel 1354. Meat is injected into the pressure vessel via conduit
1362 at a selected mass flow rate. Carbon dioxide and water is
injected via conduit 1356 at selected flow rates. The meat will
become exposed and blend with the water and carbon dioxide in
vessel 1354 through the use of agitator 1412. The meat will
substantially fill vessel 1354 to a predetermined level before gate
valve 1388 is opened. Carbon dioxide will be lighter than the meat
and water contained within vessel 1354 and will therefore tend to
accumulate at the upper end of vessel 1354. Port 1422 is located
and arranged to allow extraction of the carbon dioxide gas via
conduit 1370. Compressor 1390 can elevate the pressure by about 25
psi to about 50 psi and then recycle the compressed gas via conduit
1396, and conduits 1348 and 1400. The carbon dioxide gas will
reticulate upwardly and blend with the meat within pressure vessel
1354. The meat is agitated by apparatus 1412. The carbon dioxide
gas will mix with the water contained within vessel 1354, forming
acidic carbonic acid. The carbonic acid will destroy or weaken
pathogens that may be present at the surface of the meat. After an
effective period, the meat can be extracted from pressure vessel
1354 via conduit 1414, and transferred into vessel 1408 at a
selected rate about equal to the rate of meat that is injected into
vessel 1354. The method of transfer from the relatively lower
pressure vessel 1408 to the higher pressure in conduit 1308, is by
way of a rotating screw 1454. The transfer mechanism can both
transfer the meat and also elevate the pressure of the contents
within conduit 1308. If so desired, LFTB having been processed
according to the process described in association with FIG. 4, can
be injected via port 1406, so as to blend with the meat in vessel
1408.
[0127] Conduit 1380 with valve 1372 is shown at the upper end of
pressure vessel 1354. Valve 1372 can selectively allow injection of
any liquid or gas, such as carbon dioxide at an elevated pressure,
into vessel 1354 when valve 1372 is switched to an open position.
Conduits 1362 and 1356 are shown with valves 1374 and 1376.
Conduits 1398 and 1400 are shown with valves 1382 and 1384, and
conduit 1370 is shown with valve 1468. Additionally, conduit 1406
is shown with valve 1386, and a gate valve 1388 is shown in conduit
1414, wherein the valve 1468 is interposed between vessel 1354 and
vessel 1408. The purpose of valves 1376, 1374, 1372, 1468, 1382,
and 1384, and gate valve 1388, is to isolate vessel 1354 so as to
be able to retain the meat within vessel 135 for an effective
period. The meat, water, and carbon dioxide are injected into
vessel 1354 via conduits 1362 and 1356 at a pressure of not more
than 500 psia after closing gate valve 1388 and valves 1382, 1382,
1383, and 1468. After substantially filling vessel 1354 with meat,
water, and carbon dioxide, valves 1376 and 1374, and 1372 can be
closed. In this condition, the pressure inside vessel 1354, is
approximately 500 psia. Valve 1372 remains ready to open so that
high pressure carbon dioxide gas and/or liquid carbon dioxide can
be transferred into vessel 1354. Carbon dioxide gas transferred
through conduit 1380 will be at such pressure and volume so as to
elevate the pressure within vessel 1354, to a pressure
substantially higher than 500 psia, such as about 850 psia or even
as high as about 1050 psia or more. By doing this, the pH of the
carbon dioxide and water (carbonic acid), will decrease in a short
amount of time to a level of about 2 to about 3 pH. The increase in
pressure can be produced suddenly to produce a sudden and
substantial pH reduction. When sodium chloride or other pH
adjusting substance is present, the pH may be as low as about 1 to
about 2. A sudden lowering of the pH of the liquid in contact with
the meat can cause a rapid death of pathogens, and decontamination
of the meat. Other pathogens such as salmonella can also be killed
in this manner. By processing meat with the multiple stage methods
disclosed herein in association with FIG. 23, the pathogen
organisms that may be present on the surfaces of the meat can be
killed without causing excessive damage to the meat. The general
principle in the embodiments disclosed in association with FIG. 23
is to weaken organisms in a first vessel, by exposure to an
environment that will cause the organisms to expend significant
amounts of energy in their normal homeostasis process of
maintaining pH, and then, in a second vessel, exposing the
organisms to a second, more severe condition, thereby causing death
to the organisms. The process can allow extended exposure in the
first vessel at a relatively lower pH of about 2 to about 5 during
which the organism is forced to use high levels of energy while the
meat is substantially unaffected, followed by a relatively brief
exposure at a very low pH of about 1 to about 3 that will kill the
bacteria in a short time.
[0128] Referring now to FIG. 24, a cross section through one
embodiment of an apparatus that can be used to carbonate water at
high pressure of about 200 psia to about 2000 psia, is shown. A
pressure vessel 1518 is connected to a high pressure water supply
via conduit 1500, and a high pressure carbon dioxide supply via
conduits 1516, 1510, and 1512. A conduit 1532 with valve 1524 is
located at the base of pressure vessel 1518, and a conduit 1520
with valve 1528 is located at the upper end of pressure vessel
1518. Water is transferred at high pressure through conduit 1500,
by high pressure pump 1504. Water is transferred to pump 1502 via
conduit 1506. Water under high pressure substantially fills
pressure vessel 1518. High pressure carbon dioxide gas is injected
into vessel 1518, via conduit 1516, and through conduits 1512 and
1510 opening directly into vessel 1518. Carbon dioxide gas injected
in such a manner will cause carbon dioxide to dissolve in the water
1524. Excess carbon dioxide gas will accumulate in the space 1508
above the level of the water. Conduit 1520 is connected to a
compressor such that carbon dioxide gas can be withdrawn from
vessel 1518, via conduit 1520. After compression, the carbon
dioxide can be recycled by injection through conduit 1516. Carbon
dioxide gas can be recycled to ensure that the water 1524 is
saturated with carbon dioxide gas, forming carbonated water and
carbonic acid, that can be transferred from vessel 1518 via conduit
1532, into any apparatus arranged to decontaminate goods with the
use of carbonic acid. Carbonated water that is selectively
withdrawn from vessel 1518 as required by opening valve 1524, can
be used in equipment disclosed herein, as an alternative or in
addition to carbon dioxide gas.
[0129] Referring now to FIG. 25, an apparatus used to decontaminate
goods, such as meat, is illustrated. The apparatus can be used as a
low pH stage apparatus following a high pH stage apparatus. A
pressure vessel 1624 is mounted on frame members 1644. End piece
1628 is connected to pressure vessel 1624 by hinge 1626, such that
when in a closed position, flanges around the circumference of
pressure vessel 1624, and end piece 1628, create an airtight seal.
Clamps (not shown), are provided to ensure that pressure vessel
1624 and end piece 1628, are held firmly and securely together in
an airtight and liquid tight condition. Ports with valves are
provided on vessel 1624 that can enable complete isolation and
sealing of vessel 1624. Frame 1630 is encased within vessel 1624.
Frame 1630 is attached to shaft 1632 connected to variable speed
motor 1638. Frame 1630 is arranged such that a cage 1648 can be
securely located within the frame 1630, and readily removed there
from so as to allow replacement with similar cages. Cage 1648 can
be pre-loaded with goods, such as meat or vegetables, prior to
placement in frame 1630. Frame 1630 is attached to drive shaft that
penetrates pressure vessel through opening 1642. Opening 1642 is
configured to be gas tight around shaft 1632. Motor 1638 drives
shaft 1632, and therefore frame 1630. Conduits 1602 and 1608 are
fitted with valves 1604 and 1610, respectively. Valves 1604 and
1610 are arranged to be operated allowing atomized water
(carbonated or otherwise) to be sprayed into the vessel 1628.
Conduit 1614 and valve 1616 are connected to a vacuum pump and/or a
source of high pressure carbon dioxide gas or liquid. Conduit 1618
is fitted with valve 1620 and provides communication between dish
1636 in vessel 1624 and a waste disposal vessel (not shown) that
will allow for the removal of excess liquids that accumulate in
dish 1636. Goods, such as meat, can be loaded into cage 1648. After
loading cage in vessel 1624, and closing and sealing vessel 1624,
vessel 1624 is evacuated by opening valve 1616 and applying a
vacuum to conduit 1614, while valves 1620, 1604, and 1610, are in a
closed position. After evacuation of vessel 1624, carbon dioxide
gas is injected via conduit 1614, at a pressure of at least about
500 psia. Motor 1638 is switched on so as to drive shaft 1632,
thereby rotating frame 1630 and cage 1648. Atomized water can then
be sprayed into vessel 1624, via conduits 1602 and 1608, in such a
manner so as to ensure the surfaces of the goods are wetted. Carbon
dioxide can dissolve in the atomized water, forming carbonic acid.
The pressure within vessel 1624 may be at any pressure, such as
greater than about 500 psia, to lower the pH to an effective level.
This process can be continued for an effective time period, so as
to ensure that substantially all pathogens, or unwanted bacteria
that may be on the surface of goods in cage 1648, are killed.
Following this process, the pressure of gas in vessel 1624 can be
reduced to a pressure about equal to atmospheric pressure, and the
vessel 1624 can be opened to allow removal of cage 1648 and
subsequent replacement with another cage, similarly loaded with
goods. At this time, valve 1620 can be opened to allow liquids that
may have accumulated in dish 1636 to be removed via conduit 1618
away from vessel 1624. Following replacement of cage 1648, and the
resealing of vessel 1624, valves 1620, 1604 and 1610, can be closed
and the evacuation of vessel 1624, can be repeated. Carbon dioxide
is injected into vessel 1624, followed by spraying atomized water
through conduits 1602 and 1608. Alternatively, water followed by
carbon dioxide can be applied.
[0130] Referring now to FIG. 26 a carousel 1746 assembly is
arranged with five pressure vessels 1712, 1714, 1716, 1718 and
1724. Carousel 1746 indexes by rotating in a counterclockwise
direction. Each pressure vessel can be constructed in a manner
similar to the one that is described above and associated with FIG.
25, such that cages can be loaded, processed in the manner
described above, and subsequently unloaded by an automated off
loader. A compressor 1726, pressure vessel 1734, conduits 1740 and
1738, with valves 1736 and 1728, respectively, and conduit 1732
with valve 1730 connected to a carbon dioxide supply, are shown
connected to each vessel. Drive motors 1762, 1744, 1750, 1752, and
1754 are connected to the frames inside of each vessel similar to
the one shown in FIG. 25, via drive shafts 1764, 1748, 1760, 1758,
and 1756, respectively.
[0131] The carousel assembly shown in FIG. 26 is arranged to rotate
in an indexing manner so that after each indexing motion, a
different vessel is arranged to carry out a different operation.
Indexing refers to incrementally moving the carousel assembly about
its axis so that after each movement, a different vessel is aligned
with the loading and offloading conveyors. For example, the
carousel assembly indexes after the loading of cage 1720 on
conveyor 1704 into vessel 1712, while vessel 1724 is unloaded of
cage 1722. End piece 1766 of vessel 1712 is then closed so as to
seal the vessel 1712 in an airtight manner and carousel 1746 is
then indexed in a counterclockwise direction so that the vessel
1724, which has just been unloaded of cage 1722 by unloading
conveyor 1708, is then located in line and adjacent to loading
conveyor 1704 in readiness to accept a new cage. Vessels that are
not being loaded or unloaded can be in different stages of the
processing described in association with FIG. 25. So for example,
at station where vessel 1714 is located, carbon dioxide can be
added. At station where vessel 1716 is located, driver motor 1750
can be rotating cage within vessel 1716, simultaneously being
sprayed with water. At the station where vessel 1718 is located,
vessel 1718, can be drained of water. It should also be appreciated
that fat content and water content in meat can be controlled by
adjustment of added water and carbon dioxide conditions.
[0132] Conveyor 1708 can be enclosed in a tunnel that is flooded
with chilled filtered air, at a positive pressure, and wherein the
enclosed tunnel connects directly to a temperature controlled
packing room, where processed and decontaminated goods can be
packed after decontamination, and in such a manner that other
potential vectors of recontamination are minimized.
[0133] For the decontamination of plant material, wherein the plant
material contains stomata; microorganisms, including bacteria, can
inhabit the interior of the plant material by gaining access
through these stomata. The stomata can close, thereby trapping the
microorganisms in a location where it is difficult for
decontamination agents to treat these microorganisms. Therefore,
for decontaminating plant material, it is desirable to cause the
stomata to open, thus allowing the decontamination agent, including
carbonic acid, made from carbon dioxide and water at high pressure,
to reach the microorganisms contained within the stomata of plants.
The stomata can be opened prior to the treatment with the
decontamination agent. Certain applications where this may be of
use is in the decontamination of cabbage and broccoli, for
example.
[0134] In certain instances, the processes disclosed herein can be
used to fully pasteurize and eliminate the presence of pathogens
from goods, such as meat. In these instances, the processed goods
can be inoculated, after elimination of the harmful pathogens, with
generic or spoilage bacteria that are not harmful to humans.
[0135] Referring now to FIG. 27, equipment that can be used for
handling, processing and transporting meat is illustrated. A meat
pump 1806, has inlet conduits 1800, 1802, and 1804 and an outlet
conduit 1808, that can attach to a tank 1814 carried on a trailer
truck. Conduit 1808 is arranged to transfer meat pumped by pump
1806 into tank 1814 through a wall that separates tank 1814, from a
refrigerated room 1812. Tank 1814 can be mounted on trailer 1820.
Tank 1814 with trailer 1820 is attached to a prime mover 1816, such
as a truck vehicle. Tank 1814 can be isolated by closing a valve on
conduit 1810, and then the vehicle can travel along any highway or
road, to another destination where the meat contained in tank 1814
can be removed and then further processed. A fat measuring device
1822, such as a model supplied by AVS-Safeline, can be located on
conduit 1808 and used to measure the fat and lean content of meat
transferred into tank 1814.
[0136] Referring now to FIG. 28, a mobile decontamination unit is
illustrated. The unit can be used to apply a high pH alkaline
solution to the surfaces of meat, such as boneless beef. The unit
can also allow for immersing the meat in a low pH solution, wherein
the low pH solution uses carbonic acid generated by combining
carbon dioxide and water at high pressures. Immersion in alkaline
solution ensures that the external surfaces of the meat are covered
with the alkaline solution. The temperature of the meat may be
about 40 degrees F. Immersion in a vessel containing sufficient
alkaline solution can ensure the complete exposure of meat to the
solution. As an alternative, the solution may also be sprayed onto
the meat surfaces. The alkaline solution may have a pH ranging from
greater than about 7 to about 14. Most of the bacteria can be
killed using a pH of about 12 to about 14. However, it is
anticipated that any bacteria that remains alive will become
acclimatized to the alkaline solution. After exposure of the meat
to the alkaline solution for an effective period of time, the meat
can then be immersed in a low pH, acid solution. Any suitable acid
can be used, including carbonic acid generated by dissolving carbon
dioxide in water at high pressure. Acid solutions can be produced,
ranging in pH from about 1 to less than about 7. By exposing the
meat to a high pH alkaline solution, followed by exposure to a low
pH acid solution, so that the difference between the highest pH and
the lowest pH ranges anywhere from about 1 to about 13, the meat
can be decontaminated of bacteria.
[0137] Referring once again to FIG. 28, an outer exterior
insulating cover 1900 encloses a cavity 1904. Cavity 1904 may
contain compressed gas or liquid 1906, including carbon dioxide or
ammonia gas. The carbon dioxide and ammonia are pH modifying
agents, meaning carbon dioxide can render a liquid acidic, and
ammonia can render a liquid alkaline. The exterior cover 1900 also
encloses an interior vessel 1902. The cavity 1904 is interposed
between the outer exterior insulating cover 1900 and the vessel
wall 1902. Meat 1910 is shown located within the interior of vessel
1902. Impeller 1912 is driven by a driver (not shown). A compressor
or pump (not shown) with appropriate piping to the vessel 1902 can
provide the force to move the pH modifying agent 1906 to and from
cavity 1904 and vessel 1902. Valves can be provided where
appropriate to allow the transfer of agent 1906 from cavity 1904
and into vessel 1902 at a controlled rate so as to provide the
desired temperature and/or pH within vessel 1902. The compressor
can also be used to compress excess gas that may accumulate in
vessel 1902 and return compressed gas to cavity 1904 for storage.
Impeller 1912 can mix the meat, thus ensuring the meat is exposed
to the pH modifying agent. Impeller 1912 can be driven by any
suitable driver and arranged to slowly agitate and mix the meat
1910 so as to expose substantially all the surfaces of the meat.
The ammonia gas can react with water present in the meat to form
ammonium hydroxide, which is a powerful alkali. Alternatively,
water and ammonia can be added. The contents of vessel 1902 can,
therefore, be exposed to ammonium hydroxide, a powerful alkali that
can increase the pH at the surface of meat contained in vessel 1902
to a pH level of about 12 to about 14. Alternatively or
additionally, a vessel containing compressed or liquid carbon
dioxide may be provided such that, after processing with ammonia
for an effective period of time, the contents of vessel 1902 can be
exposed to carbon dioxide, which will form carbonic acid when
coming in contact with water present in the meat. Alternatively,
water and carbon dioxide can be added. Carbon dioxide and water can
be added in amounts and under conditions to control the water
content and fat content of meat, if so desired. The carbon dioxide
gas (or liquid) may be provided at an elevated pressure, such as
about 300 psia to about 500 psia or greater, thereby allowing
production of carbonic acid. The meat contained in vessel 1902 can
be processed while being transported, in a way that exposes the
surfaces of the meat to a high pH, followed by a low pH. In one
embodiment, the high pH can be in the range of about 12 to about
14, followed by a low pH in the range of about 1 to about 3.
Additionally, other substances disclosed herein may be provided to
adjust the pH. Such exposure to a high pH followed by a low pH will
be lethal to bacteria. The exposure time to ammonia gas can be
optimized so as to ensure that all bacteria are killed when the
meat is secondly exposed to the low pH carbonic acid. Excess gasses
used in vessel 1902 can be collected through a port (not shown)
which can be located at the upper side of vessel 1902, compressed,
and returned to the respective storage cavities or vessels and then
reused as required or alternatively vented to the atmosphere.
[0138] The processes disclosed herein can provide an effective
means for decontaminating meat, including boneless beef, by firstly
exposing the meat to a very high pH anywhere in the range from
about 12 to about 14 for a selected or effective period of time
followed by exposure to a low pH anywhere in the range from about 1
to about 3 for a further selected or effective period of time. Such
a process can be capable of killing microorganisms, and
decontaminating or pasteurizing the meat while also maintaining the
meat at a low temperature of about 40 degrees F. Additionally,
carbon dioxide and water can be provided in amounts and under
conditions described herein, to control the water content and fat
content in meat.
[0139] Referring now to FIG. 29, one embodiment of a method
according to the present invention is illustrated as a block
diagram. For any process that advantageously uses carbon dioxide to
generate carbonic acid, the process can be supplemented with the
addition of an alkali metal chlorite agent, represented by block
2000. Any suitable alkali metal chlorite can be used, including
potassium chlorite and sodium chlorite. The alkali metal chlorite
may be supplied as a solid or in solution. The alkali metal
chlorite addition, represented by block 2000, can take place prior
to carbon dioxide addition, represented by block 2004. Any amount
of alkali metal chlorite added to carbonic acid can reduce the pH
below what is capable by carbon dioxide alone. In practice, the
alkali metal chlorite agent should be applied to cover as much of
the meat surface as is practicable, and also to ensure that the
lowering of the pH is effective at inactivating the
microorganisms.
[0140] Once an alkali metal chlorite has been applied, the meat
containing the alkali metal chlorite is transferred to a pressure
vessel, represented by block 2002. The pressure vessel can have an
inlet and an outlet, and means to transfer the meat from the inlet
to the outlet. Transfer apparatus may include conveyors, belts, and
the like. However, meat can transfer through a vessel utilizing the
force of gravity. The pressure vessel can be fitted with
instrumentation to monitor the amount of meat passing the inlet and
the outlet. The pressure vessel may also be fitted with fat and
water measuring devices at all inlets and outlets that can measure
the fat and lean content, and water, of the meat. The pressure
vessel may also be fitted with any other suitable instrumentation
to monitor the pressure and/or temperature and the liquid level in
the pressure vessel. The pressure vessel may have any number of
additional inlets for the addition of agents, including alkali
metal chlorites, carbon dioxide, and water. Every inlet can be
fitted with a measuring instrument to measure the amount of agent
passing through the inlet. Every inlet can be fitted with a
metering device, such as a control valve, to accurately meter the
amount of agent passing into the pressure vessel.
[0141] Although FIG. 29 shows that alkali metal chlorite addition
is ahead of the transfer of meat to the pressure vessel, block
2002, the alkali metal chlorite addition, block 2000, may take
place after the meat is transferred to the pressure vessel, block
2002. The alkali metal chlorite addition step, block 2000, can
occur apart from the carbon dioxide addition step, block 2004, so
that alkali metal chlorite and carbon dioxide are not prematurely
mixed with one another. In some embodiments, alkali metal chlorite
addition can take place before carbon dioxide addition. In other
embodiments, alkali metal chlorite addition can take place after
carbon dioxide addition, and it may be possible that alkali metal
chlorite addition can take place at the same time with carbon
dioxide addition. However, in this case, the alkali metal chlorite
is introduced via a separate supply conduit from carbon dioxide, so
as to not prematurely cause a reaction of the alkali metal
chlorite, thus wasting the chlorite. The pressure vessel may be
fitted with a mixer to more adequately mix the meat to expose all
the surfaces to the alkali metal chlorite and carbon dioxide, and
water. The pressure vessel can be devoid of substantially all
oxygen and replaced with any suitable gas, including nitrogen and
carbon dioxide, for example.
[0142] Carbon dioxide can be added in sufficient quantities so that
the carbon dioxide together with the alkali metal chlorite and a
water phase present in or on the meat produce a carbonic
acid/alkali metal chlorite solution of sufficiently low pH to cause
inactivation of microorganisms. The carbon dioxide addition can
occur after the alkali metal chlorite addition in order to prevent
reaction between the alkali metal chlorite and the acid prior to
their exposure to the meat. In this manner, the chlorite is
conserved and used when present on the meat. The pressure vessel of
block 2002 is pressure controlled within any of the pressure and
temperature ranges described herein. Carbon dioxide addition may
take place as a solid, a liquid, a gas, or as a supercritical
fluid. The carbon dioxide is added in an amount that is effective
to cause the desired lowering of the pH to within the ranges
described herein effective to inactivate microorganisms, such as
bacteria.
[0143] Referring once again to FIG. 29, the water addition step,
represented by block 2006, may take place before, after, or during
the addition of the alkali metal chlorite, block 2000. FIG. 29
should not be construed as limiting the order of the water addition
step, as FIG. 29 is only one embodiment of the invention. Water
addition, block 2006, may take place before, during, or after the
meat transfer to a vessel, block 2002. Alternatively, water
addition, block 2006, may take place before, during, or after
carbon dioxide addition, block 2004. The water can be measured and
metered to achieve the intended effect of lowering the pH, and
additionally, water may be metered to provide the meat with any
previous or anticipated moisture loss by compensating for any
dehydration that may occur throughout all stages of processing. To
this end, the pressure vessel may be fitted with moisture content
analyzers for measuring the moisture content of the meat entering
the pressure vessel as well as for measuring the moisture content
of the meat exiting the pressure vessel.
[0144] In addition to alkali metal chlorite agents, any other
suitable agent, such as sodium chloride, may also be added before,
during, or after any of blocks 2000, 2002, 2004, and 2006.
[0145] The use of a "multiple hurdle" strategy for pathogen
decontamination of goods, such as meat, is provided. According to
the invention, each decontaminating hurdle may have a limited, but
nevertheless unsubstantial deleterious effect on the quality of the
food, and it is therefore desirable to minimize the intensity of
each treatment. Multiple hurdle is a strategy with a series of
multiple treatments of minimized intensity, thereby minimizing the
overall combined deleterious effect, as compared to a single more
aggressive treatment. For example, irradiation that pasteurizes the
meat in a single treatment is more deleterious to the meat when
compared to multiple, albeit, lesser intense treatments. Such a
single treatment with irradiation, in the presence of air, would
cause oxidation or rancidity that can otherwise be reduced with
multiple treatments. Additionally, a multiple hurdle strategy may
create virulent strains of a pathogen, not by "natural selection"
but by "multiple hurdle selection". According to the invention,
each hurdle is followed by a subsequent treatment within an
effective period of time that does not allow the pathogens to adapt
to an enhanced acid tolerance that would enable survival of the
pathogen in a subsequent treatment.
[0146] The multiple hurdle processes herein disclosed provide for
the decontamination of goods, such as meat, without substantial
deleterious effect on the meat quality. The meat is packaged
directly after decontaminating so as to reduce the possibility of
recontamination. The processes also enable reproducibility,
according to HACCP standards, using agents, such as "processing
aids" as defined and allowed by USDA. The USDA definition of
"processing aids" are those specified agents, used according to a
HACCP method in a specified process, in a USDA acceptable
decontamination process and wherein USDA allows the use of agent(s)
without the requirement to disclose the use or presence of the
agent(s) in the essential information shown on a label affixed to
the finished and packaged meat product.
[0147] Sodium ions, naturally present in meat, such as in lean beef
that contains about 0.1% sodium chloride, can assist in lowering
the pH of the carbonic acid. Additionally, the natural acid
"buffering effect" of meat can be minimized by adding an
overwhelming amount of pressurized carbon dioxide, combined with
any added sodium compound(s), including sodium chlorite. These
conditions can cause production of a low pH acid at the meat
surfaces, which is lethal to pathogens when the pathogens remain in
this environment for an effective period of time. Mass-flow control
of meat through the pressure vessel, in combination with control of
carbon dioxide density and pressure, sodium ions, and water, within
the vessel, enables the control of pathogens present at the meat
surfaces. The exposure period is related to the residence time
within the treatment vessel, which is determined by adjusting the
mass flow rate of meat through the vessel. The low pH condition,
can be enabled upon positive displacement pumping creating the
desired high pressure and the very low pH condition can be
terminated by pressure reduction upon extraction of the meat from
the treatment vessel and into a controlled lower pressure vessel.
Such pH control enables use of an acid shock treatment (AST) that
is highly lethal to pathogens, while the deleterious effects to the
meat, that over exposure to a pH of about 2 would otherwise cause,
are substantially limited. This continuous decontamination process
can be used to treat meat in combination with other suitable
bactericidal treatments, such as irradiation.
[0148] The system according to the invention can measure the mass
flow of the meat and proportionately add water and carbon dioxide.
The amount of added water can be adjusted to compensate for
moisture losses due to dehydration, and/or to ensure product
labeling is not required.
[0149] In another embodiment, meat or vegetables, can be treated
with ethanol and/or lactate prior to exposure to carbonic acid. The
ethanol and/or lactate can be applied to the food, in a manner that
will ensure exposure of substantially all surfaces to the
ethanol/lactate, prior to transfer into a pressure vessel
containing carbon dioxide and water, and at a pressure of about 550
psig or greater, and at a temperature of about 40.degree. F. Under
such conditions, carbonic acid can have a pH of about 2 to about 3.
The combination of ethanol and/or lactate with carbonic acid
creates an environment lethal to pathogens, including any
acid-adapted Escherichia-coli 0157:H7. When E. coli is exposed to
an ethanol, of about 5%, and lactate combination at a pH of about
3, the collapse of the cytoplasmic pH can occur suggesting that
cell membrane permeability to protons is compromised and/or the
capacity to pump protons out of the cell is reduced, causing death
to the bacteria. The conditions when goods, such as meat, are
exposed to liquid and/or dense vapor carbon dioxide, can be
comparable. The high solvent property of liquid carbon dioxide can
be a perturbant (similar to that of ethanol) to the cell membrane
and the pH of carbonic acid (formed by combination of carbon
dioxide and water) at about 36 degrees F., and 600 psig is about 3.
Therefore, when the goods are exposed to liquid carbon dioxide
and/or very dense carbon dioxide vapor, the population of E. coli
(and other bacteria) can be reduced by about 4 log, in about 5
minutes of exposure.
[0150] The density of the pressurized carbon dioxide can be at
least about equal to or higher than about 20 lbs/cubic foot, such
that when the meat and dense carbon dioxide are in contact and
located together in a treatment pressure vessel and agitated, the
carbon dioxide will assist in opening and separating any flaps,
slits, cracks and/or leaves that may be enclosing pathogens in a
location protected from exposure to the lethal agent or combination
of agents intended to kill the pathogens. Following treatment with
carbonic acid, as disclosed, the meat can be exposed to a low
dosage irradiation source such as e-beam, or x-ray of sufficient
intensity to kill substantially all remaining weakened
pathogens.
[0151] Referring now to FIG. 30, an apparatus arranged to process
goods, such as meat including boneless beef, is schematically
illustrated. Meat 2154 is loaded into hopper 2162. Hopper 2162 is
connected to a horizontal conduit 2138. An auger 2166 is mounted
within conduit 2138, and is attached to a drive motor 2172. Auger
2166 can carry meat through conduit 2138. A series of ports, 2434,
2142, 2128, and 2130, are connected to the horizontal conduit 2130
with valves 2116, 2102, 2156, and 2106, respectively, arranged to
open and close when desired. Ports 2434 are arranged to allow a
solution of sodium chlorite, which may be atomized to create a
"fog," that is then transferred into conduit 2138 so as to contact
the meat as the meat is transferred through conduit 2138 to expose
the meat to the solution of sodium chlorite. Ports 2128 and 2130
are arranged to transfer carbon dioxide gas, so as to substantially
displace all air that may be present within the conduit 2138. After
transfer along the conduit 2138, the meat 2154 is deposited into
hopper 2158, which is mounted directly above positive displacement
pump 2110. Port 2174 is attached to a vacuum source so as to enable
removal of gas that may be carried with the meat. The positive
displacement pump 2110 is connected to a variable speed drive motor
(not shown) so that meat 2154 can be pumped, at an elevated
pressure of about 550 psig or greater, into pressure vessel 2164.
Pressure vessel 2164 is horizontally disposed and is fitted with an
auger 2168, connected to drive motor 2170. Ports 2132, 2140, and
2136 are connected to pressure vessel 2164 and are fitted with
valves 2108, 2114, and 2104, respectively, that are arranged to
open and close automatically. Port 2132 is arranged to transfer
liquid carbon dioxide, into pressure vessel 2164 at a pressure of
about 500 psig and port 2140 is arranged to extract liquid carbon
dioxide from pressure vessel 2164. Port 2136 allows the escape of
carbon dioxide gas, which can then be collected, and recycled into
ports 2128, 2130 and 2132. A positive displacement pump 2112 is
arranged to pump the meat into the next processing equipment, such
as a grinder. The apparatus shown in FIG. 30 enables the
decontamination of meat, such as boneless beef, by exposing the
surfaces of the meat to a very low pH acid having a pH of about 1
to about 2, for an effective period of time. The pH is achieved by
mixing the meat with liquid carbon dioxide after having treated the
surfaces of the meat with sodium chlorite. The pH of carbonic acid
at about 550 psig is about 2 to about 3; however, with the addition
of sodium ions (in the form of sodium chlorite solution), the pH
can drop to about 1 to about 2. When the pressure is lowered after
extraction of the meat, the pH can be elevated to about 5 to about
6. Meat can be treated for any selected period of time by
controlling the mass flow of the meat into pressure vessel 2164 by
pump 2110, and the speed of auger 2168 which transfers and mixes
the meat with liquid carbon dioxide prior to direct transfer into
hopper 2160. The meat from hopper 2160 is then transferred by pump
2112.
[0152] After grinding, the meat can be further treated by exposure
to irradiation, including any e-beam treatment, while still being
retained within a conduit substantially excluding oxygen of less
than 5% by volume, or less than 3% by volume or less than 1% by
volume or less than 300 ppm by volume.
[0153] Referring now to FIG. 31, a cross section through an
apparatus that can be used to decontaminate goods, including meat,
is shown. A vertically disposed pressure vessel 2200 is arranged
with a series of ports that communicate directly with the interior
of vessel 2200. A centrally and vertically disposed stirring
mechanism 2238 is attached to drive motor 2250 such that stirring
mechanism 2238 rotates slowly in the direction shown by arrow 2212.
A grinding plate 2228 is mounted in conduit 2240 with space allowed
on the upstream and downstream sides of the grinding plate 2228. An
e-beam generator 2256 can be located upstream of grinding plate
2228. Goods, such as meat, passing through conduit 2240 can
therefore be irradiated before grinding. Exposure of goods to an
e-beam can cause the death of any pathogens that may have survived
the potentially lethal effects of the processing taking place in
vessel 2200. The e-beam generator 2256 is shielded so as to protect
any persons required to be present during the operation of the
e-beam generator. A suitable irradiation generator includes a
PRECISIONSCAN.TM. 500 Model, manufactured and sold by the Titan
Corporation, of San Diego, Calif. 92121. Conduit 2240 is connected
to an expansion vessel 2234 and a conduit 2232 is connected
downstream of grinder 2228. Goods, including LFTB, can be pumped
into conduit 2240 via conduit 2232. Goods pumped through conduit
2232 can be decontaminated prior to their introduction into conduit
2240. Other materials, including ingredients, that may be sensitive
to decontamination by e-beam irradiation, and that may have been
decontaminated by another method, such as by heat, can also be
transferred into conduit 2240 at a controlled mass flow rate. A
compressor 2218 is connected to an inlet conduit 2216, an outlet
conduit 2224 and a pressure release conduit 2220. Pressure release
conduit 2220 is fitted with a pressure release valve 2222, that
allows the escape of carbon dioxide gas when the gas exceeds a
pre-determined pressure setpoint. Carbon dioxide gas compressor
2218 extracts carbon dioxide gas via port 2248 from within vessel
2200. After compression of the carbon dioxide gas by compressor
2218, the compressed gas is then re-circulated into pressure vessel
2200, via conduit 2224 through ports 2226 and 2227 at the base of
the vertically disposed pressure vessel 2200. Meat, such as
boneless beef, is injected into the pressure vessel 2200 via
conduit 2208 at a selected mass flow rate. A proportional quantity
of carbon dioxide and water is injected via port 2202 into vessel
2200. The meat can be exposed to and blend with the water and
carbon dioxide in vessel 2200. The meat will fill chamber 2200 to a
pre-determined level before grinder plate 2228 commences grinding.
In this way, the meat can be retained within pressure vessel 2200,
for any selected and effective time. Carbon dioxide gas will be
less dense than meat and water, and will therefore accumulate at
the upper end of the vertically disposed pressure vessel 2200. Port
2248 is located and arranged to allow extraction of the dense
carbon dioxide gas via conduit 2216. Compressor 2218 can raise the
pressure of carbon dioxide by about 25 to about 50 psi and then
recycle the compressed gas via conduit 2224, and through ports 2226
and 2227. The dense carbon dioxide gas can reticulate upwardly and
blend with the meat held within pressure vessel 2200, which is
agitated by agitator 2238, and in so doing can ensure that water
contained within vessel 2200 is saturated with carbon dioxide,
forming highly acidic carbonic acid. After an effective period, the
meat can be extracted from the pressure vessel 2200 via conduit
2240, and pass by grinder 2228, that can be arranged to grind at a
selected rate about equal to the rate of meat injected via conduit
2208. Conduit 2270 with valve 2262 is located at the upper end of
pressure vessel 2200. Conduit 2270 can allow injection of any
liquid or gas, such as carbon dioxide, at an elevated pressure,
when valve 2262 is switched to an open position. Conduits 2208 and
2202 have valves 2264 and 2266, respectively. Ports 2226 and 2227
have valves 2272 and 2274, and conduit 2216 has valve 2280.
Additionally, conduit 2232 has valve 2276, and conduit 2240 has
valve gate 2278, wherein valve 2278 is interposed between grinder
2228 and vessel 2200. The purpose of valves 2264, 2266, 2262, 2280,
2272, and 2274, and gate valve 2278, is to isolate vessel 2200.
Meat, water, and carbon dioxide are injected into vessel 2200 at a
pressure of about 500 psia after closing gate valve 2278 and valves
2272, 2274, 2280. After substantially filling vessel 2200 with
meat, water and carbon dioxide, valves 2266 and 2264 can be closed.
In this condition, the pressure inside vessel 2200, is about 500
psia. Valve 2262 can be operated so that high pressure carbon
dioxide gas and/or liquid can be transferred into vessel 2200.
Carbon dioxide gas transferred through conduit 2270 can be at such
pressure and volume so as to raise the pressure within vessel 2200
to a pressure higher than about 500 psia, such as about 850 psia to
about 1000 psia. If required supercritical carbon dioxide can also
be transferred into vessel 2200 via conduit 2270. By so doing, the
pH of the carbonic acid and water at about 500 psig to about 850
psig, will decrease in a short amount of time to less than about
3.The increase in pressure can be produced suddenly to have a
sudden and substantial pH reduction. When the pH of the liquid in
contact with the meat is lowered, the reduction in pH can cause the
death of pathogens, and decontamination of the meat. Other
pathogens such as salmonella can also be killed in this manner. In
addition, an e-beam generator 2256 can be arranged to irradiate the
meat after processing in vessel 2200, and before grinding. The
intensity of the electron beam generated by generator 2256 can be
adjusted so as to enable goods in conduit 2240 to be exposed to the
minimum intensity while still having sufficient capacity to kill
any pathogens that may have survived the treatment in vessel
2200.
[0154] The process of e-beam irradiation has been used to kill
pathogens on goods after packaging, therefore requiring that the
packaging be also subjected to the e-beam irradiation. This results
in an inefficient use of the expensive irradiation process.
Packaging materials can be kept clean and without contamination by
other less expensive decontamination processes (such as with the
application of heat or Ultra Violet C). Accordingly, by
decontaminating the goods and packaging materials separately, prior
to assembly of the goods and packaging, a substantially more
efficient method of decontamination is achieved. Efficiency is
further improved when acid shock treatment, and a reduced but
adequate application of e-beam irradiation, are combined.
[0155] Referring now to FIG. 32, an apparatus constructed for use
in decontaminating goods, such as meat, is shown. Two distinct but
sequentially employed processes are combined wherein a first
decontamination process incorporating pressurized carbon dioxide
and water is arranged to precede a second decontamination process
incorporating an electron beam (e-beam) generator.
[0156] The apparatus includes a first processing vessel 2312 having
an entry port 2368 for the meat, and an entry port 2360 for carbon
dioxide and water 2300. The vessel 2312 can be operated at a
pressure ranging from about 500 psia to about 800 psia. The vessel
2312 includes a transfer screw (not shown) to transfer the goods
from the entry port 2368 at one end of the vessel to the opposite
end. The transfer screw can additionally be configured to mix the
goods. The vessel 2312 includes a narrow section that leads to a
conduit 2338 of reduced diameter. The conduit 2338 has one or more
grinders 2310. The conduit 2338 leads into a second vessel 2304.
The vessel 2304 is operated at a reduced pressure as compared with
the first vessel 2312. The vessel 2304 is operated at a pressure
from about ambient pressure or about 15 psia to about 20 psia or
any pressure that is below the pressure in vessel 2312. The vessel
2304 has a conduit 2302 located at an upper portion to vent any
evolved gas or entrained moisture from the second vessel 2304. The
second vessel 2304 also has an exit port 2306 for the meat.
[0157] In one embodiment, liquid carbon dioxide and liquid water
are injected into port 2360 at a pressure from about 200 psia to
about 500 psia or greater. The carbon dioxide and water can be
measured and metered into vessel 2312. The amount of carbon dioxide
can be based on the pH in the vessel, or on the pressure in the
vessel, or based on the quantity of water or meat.
[0158] The horizontal vessel 2312 includes a transfer screw that
may rotate about a longitudinal axis. This screw is arranged to
cause the meat to blend and mix with the carbon dioxide and water
at a pressure of about 500 psia or greater. The screw operates at a
speed which will provide adequate retention time within the vessel
2312 to kill any microorganisms, including pathogens or bacteria,
that may reside on the meat.
[0159] An electron beam generator 2372 can be integrated so as to
enable the irradiation of meat, as the meat is transferred along
the horizontal conduit 2352 and before the goods are ground by
grinder 2310.
[0160] A blend of gases, including carbon dioxide with a small
quantity of carbon monoxide can be used. Carbon monoxide causes a
red color in pork, beef and other meats. The resultant color is a
vivid bright red and will remain bright red for several weeks and
well beyond the point in time when other red meat, not exposed to
carbon monoxide, but normally exposed to oxygen or ambient
atmosphere will normally become discolored. This discoloration is
undesirable and occurs as a result of gray-brown colored
metmyoglobin forming at the surface of the meat. Red meat intended
for human consumption may be exposed to any approved gas, such as
carbon dioxide, having a carbon monoxide content less than 0.5%.
Such a small amount of carbon monoxide would not normally be
sufficient to cause the vivid red color staining, however, the
effect of carbon monoxide is cumulative, such that when meat is
exposed for an effective period to a blend of gases containing 0.5%
carbon monoxide and 99.5% carbon dioxide, the cumulative effect can
enable the generation of the vivid red color. This can be
accomplished when a blend of gases comprising an amount of carbon
dioxide about 99.5% of the combined gas blend and an amount of 0.5%
carbon monoxide is compressed and used in the process described
herein. Accordingly, such a blend of gases can be used at such
selected pressure and temperature that will enable decontamination
as desired and can also enable color enhancement of the red meat so
as to minimize discoloration.
[0161] Referring once again to FIG. 32, from the grinders 2310, the
contents of the high pressure vessel 2312, including meat, carbon
dioxide, and water, are emptied into a low pressure vessel 2304,
via interposed conduits 2338, 2352, and 2354. The low pressure
vessel 2304 is operated at a pressure which is lower than the high
pressure vessel 2312. The pressure in vessel 2304 can be anywhere
ranging from about atmospheric pressure to slightly below the
pressure of the high pressure vessel 2312. Carbon dioxide is vented
through an outlet port 2302 from the low pressure vessel 2304. The
vented carbon dioxide may contain moisture. The decontaminated meat
is transferred out of the low pressure vessel through a port 2306
located at the lower section of the vessel 2304, and can be further
processed. Many of the components of the apparatus shown in FIG. 32
have not been discussed, but it is intended to have them operate in
the manner described in association with FIGS. 3, 5, and 23.
Processing with irradiation prior to packaging is advantageous when
compared to the costs of irradiation of the same goods in the
package. This is, in part, due to the inefficiencies created by the
relative increase in the total volume of the packaged goods. Such
increase is often at least 100% more than the volume of the goods
alone. A range of packaging materials are suitable for processing
by irradiation and are invariably more expensive than alternative
materials that will not withstand irradiation. A material such as
polypropylene can tolerate relatively high irradiation doses.
Conversely, packaging materials such as UPVC and pPVC will become
discolored and brittle. PVC will turn an unappealing brown color.
Furthermore, the use of irradiation after packaging requires the
displacement or removal of any oxygen from contacting goods, such
as meat, that contain fats, that will quickly become rancid due to
ozone production caused by the irradiation. Goods such as ground
meat or sausage can be irradiated with electron beam, x-ray or
gamma irradiation after loading in PVC, UPVC, and pPVC trays, and
prior to stretch sealing with a web of lid material which may be
low cost pPVC.
[0162] Referring now to FIGS. 33 and 34, illustrations of equipment
intended for use in the separation of lean meat from fat, are
provided. The equipment includes a grinder pump 2426, and two
vessels 2428 and 2464 to operate in the manner described below.
Grinder pump 2426 may be a modified Weiler pump Model No.1109. A
motor 2400, drives a screw (not shown) located within grinder pump
2426, via a gearbox 2404 to direct a fat stream with lean meat
through a grinding plate which may have grind apertures about 1
inch in diameter, for example. The grinding plate is located
between the mixing chamber 2420 and grinder pump 2426, and is not
shown. A stream of mostly fat containing some lean meat is
introduced through hopper 2402. A gas, such as carbon dioxide or
any other suitable gas or blend of gases, is injected into hopper
2402 through ports 2406 and 2408. Such gas is provided at a
pressure and volume that can displace air from hopper 2402. A vent
nozzle 2416 allows excess gas to escape. The vent may be fitted
with a valve to control the escaping gas. A water jacket 2410 is
provided to inject heating or cooling media for temperature control
of grinder pump 2426 and its contents. An inlet port and outlet
port, 2412 and 2414, respectively for the medium are provided. The
purpose of the jacket 2410 is to adjust the temperature of the
grinder screw housing in such a way that heat transfer will adjust
the temperature of the fat stream as it is transferred along the
screw. Any suitable media may be used as a heat exchange medium,
such as glycol. Ground fat and lean meat is transferred from
grinder pump 2426, through grinding plate and into mixing chamber
2420. A fluid comprising a blend of liquid carbon dioxide and water
is transferred along with fat and lean into mixing chamber 2420.
The fluid can be blended at a pressure of about 600 psig and the pH
of this fluid can be about 3. When combined with the fat and lean
stream, the pH may drop to less than about 2 and will therefore
assist in the decontamination of the fat lean stream. Reduction of
pH can occur as a consequence of sodium ions that are present in
the form of sodium chloride in the fat lean stream. Sodium chloride
or any other suitable salt, including sodium chlorite, may be
added. The quantity of fat lean grinds transferred into mixing
chamber 2420 may be at any flow rate and the fluid flow rate (of
the blended liquid carbon dioxide and water) may be a flow rate
that is a multiple of the grinds flow rate, and can be about
one-half to about four times the flow rate of the fat lean stream.
The combined streams of fat lean and fluid are transferred along
the conduit 2422. A separating vessel 2428 comprises a centrally
disposed tube section 2432, with an upper cone 2524, and a lower
cone 2430, both attached to tube section 2432 at flanges 2512 and
2514, respectively, in a pressure tight manner. The upper interior
end of cone 2524, includes an annular space 2444, defined by a
perforated wall located adjacent the outer wall of cone 2524,
wherein the annular space 2444 is connected to port 2442.
Similarly, at the lower interior end of lower cone 2430, an annular
space 2450 is defined by a perforated wall connected to port 2448.
The blended fat lean stream from grinder pump 2426 and fluid is
transferred into the tube section 2432. The specific densities of
water, fat, and lean meat are different and the differences in
density can be used to separate the components in vessels 2428 and
2464. The specific density of water is about 1.0. The specific
density of fat is less than 1.0, and the specific density of lean
meat is greater than 1.0. Therefore, the fat lean stream will
separate by components. Fat will move upward in cone 2524, and lean
meat that will move downward in cone 2430. The specific density of
the fluid may be adjusted (elevated) by adding sodium chloride,
sodium chlorite, or any other suitable salt. For example, sodium
chloride may be added to the carbon dioxide and water so as to
adjust the specific density to be substantially the same or
slightly less than lean meat. In this way, the fat component can
separate more rapidly. Separating lean meat from the fluid can be
achieved by extracting the fluid through the perforated section
2450 in the lower end of the cone 2430 through port 2448. Fluid can
also be extracted through port 2442 at the upper end of cone 2524.
The respective components of fat and lean are directed according to
density so that the fat component will be drawn upwardly within
cone 2524 and the lean component will be drawn downwardly through
cone 2430. Additional fluid can be extracted through manifold 2434.
The total amount of fluid extracted via ports 2442 and 2448, and
manifold 2434, can be about equal to the volume of fluid blended
with the fat lean stream in mixing chamber 2420. The separated fat
component can be transferred upwardly and into conduit 2476 and the
lean component will be transferred into conduits 2452 and
continuing into conduits 2454 and 2506. Conduit 2476 can have a
pressure relief valve 2458 at the uppermost location. Pressure
relief valve 2458 can enable the venting of excess gas according to
the pressure relief valve setting. A pump grinder 2460 can be
located between conduit 2476 and conduit 2462 leading to a second
separation vessel 2464. Pump grinder 2460 is arranged to grind the
stream therethrough, with a grind size of less than one-half inch,
for example. After grinding, the stream is transferred through
conduit 2462, and into vessel 2464.
[0163] Vessel 2464 includes an annular tube section 2490 attached
to an upper cone 2526 and a lower cone 2500, at flanges 2516 and
2518, respectively. Any lean meat in the stream transferred into
vessel 2464 will be transferred downwardly into cone 2500, and the
fat component will be transferred upwardly into cone 2526, and
ultimately through conduit 2480. Such fat can be considered a waste
stream that can be transferred to a rendering plant. Lean meat is
transferred through conduit 2502. Annular space 2484 in upper cone
2526 is in communication directly with port 2488, allowing fluid to
be extracted therethrough. Similarly, annular space 2494, located
at the lower end of the lower cone 2500, is attached to port 2498
in such a manner as to allow extraction of fluid. Fluid transferred
with the fat stream into tube section 2490 can be extracted through
ports 2488 and 2498 and via manifold 2478. Fluid extracted through
ports 2442, 2448, 2488, 2498, and manifolds 2478 and 2434, can be
connected to a common pipe 2468, that leads directly to a
compressing pump 2466, with downstream pipe 2456. Fluid thereby
collected and transferred through pipe 2456 can be filtered,
adjusted in temperature, and then transferred and measured, into
mixing chamber 2420. Lean meat transferred through conduits 2502
and 2452, are combined together in conduit 2506. This combined lean
stream product can be incorporated in the production of ground
meat.
[0164] Valves and pressure release valves can be provided on all
ports and arranged to open and close in a manner allowing transfer
of material therethrough at selected flow rates that can be
automated and controlled by a computer.
[0165] Agents for use in the present invention may include any
selected temperature and pressure controlled, liquefied or
vaporized gas or a blend of liquefied or vaporized gases including
carbon dioxide and/or any atmospheric gas(es), carbon monoxide,
ammonia or any other suitable gas or processing aid including water
or any agent(s) including sodium citrate, sodium chlorite,
tri-sodium phosphate and/or sodium chloride or any combination
thereof, that may be dissolved in water (or carried as a suspension
therein), and that can be mixed with any liquefied or vaporized gas
or gases.
[0166] Carbon dioxide, at a pressure above about 1,056 psig and at
a temperature above about 87.82.degree. F., is at the critical
temperature and pressure. Carbon dioxide cannot exist as a liquid
under these conditions. Below 1,056 psig and 87.82.degree. F.,
carbon dioxide can exist as a liquid and a gas or a saturated
vapor. The specific volume (density) of carbon dioxide at 1,056
psig is about 0.03453 ft.sup.3/lb (or 28.96 lbs per cubic foot).
The maximum density of water occurs at 39.2.degree. F. (4.degree.
C.) when 1 cubic foot weighs about 62.4 lbs. However, the density
of carbon dioxide at 40.degree. F. is about 55.99 lbs per cubic
foot. Therefore, liquid carbon dioxide can float on water at
40.degree. F. when the water is saturated with dissolved carbon
dioxide. A temperature of about 109.degree. F. is the maximum
temperature of a beef carcass following death. Fresh beef will
freeze, at least partially, when its temperature is reduced to
below about 28.5.degree. F. At about 26.degree. F. or below, fresh
meat will freeze. It is therefore desirable that the processing
temperature range for meat is maintained at above about
28.5.degree. F. and below about 109.degree. F. The density of
carbon dioxide at 28.degree. F. is about 58.58 lbs/cubic foot. The
density of fat is slightly lower than the density of water and the
density of lean meat is slightly more than the density of water. In
each case, the density of fat and beef will vary according to its
water/moisture content.
[0167] One aspect of the invention provides a method to produce
processed meats having a water content that can be controlled to
within any limits. When exposed to ambient, dry, or refrigerated
air, fresh beef will undergo dehydration at a rate of about 1% per
24-hour period. The dehydration rate can be used to calculate and
meter water used as a processing aid to compensate for the water
loss or to adjust the water content of meat to any selected level.
As indicated in a Draft Directive recently issued by the FSIS
division of the USDA, it is understood that USDA intends to impose
new regulations that will allow compensation for loss of moisture
due to such dehydration by addition of an amount of water, derived
only from water contained in an agent as a processing aid of said
agent. The natural, original weight of meat harvested from a
freshly killed carcass, cannot be exceeded by 0.5% of its natural
weight, and that any added water must be less than 0.5% of the
original, natural weight of the beef.
[0168] Referring now to FIG. 35, one embodiment of an apparatus,
constructed for the purpose of processing food products, including
meat, and in particular for separating fat from a continuous stream
of lean meat and fat, is shown. Furthermore, the apparatus is
arranged to apply suitable agents, to the stream of lean meat and
fat, that can extend the shelf-life as compared with non-processed
products by, for example, reducing the number of bacteria present
with the food product(s), such as E. coli 0157:H7, Salmonella,
Listeria Monocytogenes, and other pathogens and also by improving
the appearance and/or color of the processed meat. After
processing, the meat can be packaged immediately by direct transfer
to a packaging system, via a continuous and enclosed conduit,
without exposure to other vectors of recontamination (such as
exposure to airborne Listeria Monocytogenes) that may otherwise
reinfect the meat.
[0169] The processes disclosed herein will provide accurate
temperature control of the agents, including the meat being
processed, to below about 109.degree. F. and above about
28.5.degree. F. The pressure of any agent that comprises carbon
dioxide, or a combination of agents including carbon dioxide, will
be maintained within reasonable and safe limits, including not more
than about 2000 psig. The amount of added water that remains with
the meat, after processing can be controlled at any level.
[0170] Carbon dioxide can be useful for adjusting the fat content
of a stream (or batch) of boneless meat. When carbon dioxide is
held at a temperature and pressure above the critical point, the
supercritical carbon dioxide fluid can act as a solvent that can
remove fat from lean meat. When meat is exposed to carbon dioxide
at or above the critical point, fat can be separated from lean meat
by measuring the fat content (and the moisture content) of the meat
prior to treatment, followed by treatment with accurately measured
and controlled quantities of carbon dioxide above the critical
point and at a specified temperature and pressure for an effective
time period, and also treated with water alone or together with a
processing aid, so that a specified quantity of fat can be removed
from the meat, and the moisture content can be raised to the level
before dehydration. In this way, when meat is exposed to a
controlled quantity of supercritical carbon dioxide for a selected
period of time, a predictable amount of fat can be removed from the
meat.
[0171] Referring to FIG. 35, effective time can be adjusted by
increasing or decreasing the mass flow of meat flowing through the
treatment conduit 2640. The meat is extracted via conduit 2604
after having been processed through numerous treatment sections. By
controlling the exposure time of meat to supercritical carbon
dioxide, the fat content of the meat can be adjusted. Fat is
removed from the conduit 2640 with supercritical carbon dioxide via
ports 2608 and/or 2664. These streams of mixed fat and
supercritical carbon dioxide can be separated into two streams, one
substantially fat and one substantially carbon dioxide, followed by
chilling and packaging or rendering the fat (tallow) and after
conditioning, filtering, and compressing, the carbon dioxide can be
recycled into the treatment conduit 2640.
[0172] In one aspect of the invention, a method is provided for
measuring and recording the natural weight of post mortem beef,
that is harvested from carcasses prior to significant weight loss
due to dehydration. The weight data can be used to establish a
typical weight loss due to dehydration that can occur during a
refrigeration process. The meat can be hydrated through a process
of controlled hydration from "processing aid" water contained with
any decontaminating agent.
[0173] In one aspect of the invention, a method is described for
separating fat from lean meat, and for simultaneously
decontaminating the meat by reducing the bacteria on the surfaces
of the meat with the carbon dioxide used to separate the fat.
[0174] In one aspect of the invention, a method is described for
adjusting the fat content of meat, according to a specified fat
content requirement, prior to grinding the meat to produce ground
meat with a fat content as desired and within a tolerance of about
.+-.0.25% of the desired fat content. According to the invention,
it would not be necessary to cut any fat cover from the meat prior
to processing with carbon dioxide, since the fat will dissolve in
the carbon dioxide and be removed therewith. The method of the
invention has many benefits over the existing system of ground
chuck production, for example. Firstly, the method according to the
invention requires less labor to harvest the boneless beef chuck
primal from the carcass and secondly, the method results in less
contamination. The need for the commonly practiced process of LFTB
production from the discarded fat stream produced in all beef
boning operations, is eliminated. The problems associated with
cross contamination and bacterial growth are also eliminated.
[0175] Additionally, the meat can be processed by exposing its
surfaces to carbon monoxide so as to enhance the color of the meat
wherein the carbon monoxide can be blended with another gas,
including carbon dioxide, in proportions of not more than about
0.5% carbon monoxide with the balance being substantially carbon
dioxide. Carbon monoxide can also serve as a decontaminating agent
by killing or injuring bacteria that may be present at the meat
surfaces.
[0176] Referring again to FIG. 35, a series of conduits capable of
withstanding high pressure are connected together to enable
continuous processing of meat. The apparatus is manufactured from
heavy gauge stainless steel, or any other material of construction
suitable for meat. The meat can be transferred through an inlet
conduit 2654, and ultimately after processing, extracted via
conduit 2604. Conduit 2640 is arranged with three inlet ports and
two outlet ports. Product inlet conduit 2654 is attached to an end
of conduit 2640, and has a moisture and fat analysis apparatus 2658
mounted thereon. Any suitable measuring equipment can be used, such
as an apparatus referred to as GMS, and manufactured by Thermo
Moisture Systems, of Chelmsford, Mass. 01824.
[0177] Ports 2644 and 2630 are arranged to communicate directly
with the interior of conduit 2640 via annular connections 2646 and
2666, with annular spaces 2652 and 2636, respectively, that are
connected via an annular slot or a series of slots 2650 and 2634,
respectively. Ports 2664 and 2608 allow for the removal of agents
and other materials extracted from the meat being processed in
conduit 2640. Variable speed motor 2656 is mounted at an end of
conduit 2640 and coupled directly to a shaft with paddles and screw
fixtures 2642,2626, and 2610. Processing conduit 2640 has a
restriction 2638, which is a narrowing of the vessel 2640 diameter
that can pressurize the meat being processed. Perforated section
2622 is provided and arranged to match screw profile 2626, in such
a way that solids will be forced to follow conduit 2624, and
liquids will pass through perforations into space 2628 and be
exhausted through port 2664. Valves and pressure regulators are
fitted on conduits to provide adjustments required for the
processing of meat including the control of the residence time of
the meat being processed in conduit 2640. The apparatus is
controlled by a suitable PLC or computer, enabling automated
operation according to any program developed and found to be
suitable in the processing of the meat. The PLC or computer is
arranged to control the mass flow rate of meat and any agents into
conduit 2640, and extraction therefrom and also to control variable
speed drive motor 2656. By adjusting the mass flow of meat and
agents transferred into conduit 2640, the residence time and the
effect of the agents on the meat being processed can be controlled
accurately, and in a manner that will enable optimum production
rates.
[0178] Conduit 2624 is connected to a second processing conduit
2666. A third agent inlet port 2614 is provided with connection to
the annular space 2612 and annular slot 2620. Paddles and screws
2610 are arranged to mate with the perforated section 2606 so as to
enable the extraction of liquids or gases from conduit 2660 in a
manner similar to that described for conduit 2640. At this point,
agents and meat can be divided into two streams, wherein the solid
items are transferred along conduit 2604 and through moisture and
fat measuring device 2602, and liquids and gases pass through
perforations into space 2472 and then are exhausted through conduit
2608. With the above described apparatus, meat can be processed
with agents that blend with the meat and are exhausted through
conduits 2664 and 2608. Suitable agents may be liquids, solids, or
gases or supercritical fluids, provided at any temperature and
pressure for decontamination, separation, rehydration, or for any
other purpose. The apparatus as described above can be used to
process a range of food products, including meat, such as boneless
beef, by exposure to carbon dioxide gas pressurized and heated to
greater than about 1056 psig and above about 88.degree. F. Such
carbon dioxide can be provided through ports 2644, 2630, and 2614
at a pressure of about 1100 psig and at a temperature of about
90.degree. F., and transferred into the processing conduits 2640
and 2666 to mix with the meat provided therein at a temperature of
about 35.degree. F. to about 40.degree. F. The carbon dioxide,
under these conditions, will enable the removal of fat from the
meat, which can then be removed with the processing gas or liquid
through conduits 2664 and 2608. The meat, which will then comprise
lean meat having reduced quantities of fat, can be transferred
through conduit 2624, into conduit 2666. As it is transferred
through conduit 2624, the fat and moisture content can be measured
by the measuring device 2670 prior to entry into conduit 2666.
Based upon the measured fat and moisture content, additional carbon
dioxide with a measured quantity of water can be transferred into
conduit 2666 via port 2614 to further adjust the moisture and fat
content of meat. Additionally, carbon dioxide can dissolve in water
to produce carbonic acid of low pH that will cause inactivation of
microorganisms, such as pathogens. Additional agents may be added
to further decrease the pH. Agents, including sodium chloride,
sodium chlorite, and any other salt, can be used. Carbon monoxide,
water and buffered sodium citrate or sodium chloride may be added
to carbon dioxide, for example. Carbon dioxide and water can be
adjusted in pressure and temperature according to the measured
amount of fat and moisture of the meat. Moisture can be added and
fat removed through the process to produce a finished
decontaminated product of desired fat and water, and thereafter
measured to confirm the accuracy of the process.
[0179] The embodiment of the apparatus shown in FIG. 35 can be used
as a series of similar vessels in sequence or can be used as a
single processing apparatus.
[0180] In one aspect of the invention, the beef exiting conduit
2602 may further be decontaminated using x-ray or electron beam
(e-beam). A series of these partially effective decontaminating
steps when put together can combine for complete decontamination.
Multiple hurdle decontamination may avoid damaging the meat as
compared to any single-step decontamination technique. A series of
mild decontaminating steps are as effective as a single, strong
application of any decontaminating technique without having the
detrimental effect of possibly damaging the meat.
[0181] The process provides simultaneous extraction of measured
quantities of fat from a mass flow controlled stream of meat,
enclosed in a sealed, pressurized, heated, and temperature
controlled conduit to enable production of decontaminated meat
having a selected fat and water content.
[0182] A sanitizing agent, including ozone, can be used to
disinfect the apparatus without the need to open the vessel. To
this end, the apparatus can be constructed without sharp corners to
eliminate dead areas where meat may remain stagnant. The apparatus
can be used with a clean-in-place system that does not require the
apparatus to be opened for cleaning and sanitizing. Cleaning may be
conducted with any suitable agent, such as steam or ozone.
[0183] Referring now to FIG. 36, an illustration of a pressure
vessel 2510 which can be used in the separation of fat from lean
meat using supercritical carbon dioxide, is provided. The shape of
the pressure vessel 2510 may be any suitable shape; however, in
FIG. 3, the pressure vessel 2510 is shown generally as a spherical
vessel to allow for efficiencies in construction and the capacity
to safely withstand pressures in excess of 1056 psig, and in
particular, the minimum pressure and temperature or any pressure
and temperature at which carbon dioxide can exist in its
supercritical phase. The pressure vessel 2510 is shown with a
single inlet port 2516 and three outlet ports 2504, 2524, and 2532.
However, the use of fewer or additional ports is permissible. The
vessel enables the separation of fat from lean meat, with
supercritical carbon dioxide. In the present apparatus,
supercritical carbon dioxide is blended with a stream of fat that
can contain less than about 50% lean meat. However, other
embodiments may contain greater than 50% lean meat. Prior to
introduction into vessel 2510, the stream of fat and lean meat can
be passed through a squeezing mechanism (not shown) that crushes
the fat, enabling rapid contact between the fat and the
supercritical carbon dioxide. The mixture of fat, lean meat, and
carbon dioxide is transferred along a conduit (not shown) while
being held at a pressure in excess of about 1056 psig and a
temperature in excess of about 87.degree. F., or at such pressure
and temperature that ensures the carbon dioxide transferred along
the conduit is maintained in a supercritical condition. On exposure
to supercritical carbon dioxide, fat will liquefy and blend with
the carbon dioxide. However, lean meat will remain in a relatively
unchanged condition. The mixture of supercritical carbon dioxide,
fat, and lean meat, is pumped into the vessel via port 2516.
Supercritical carbon dioxide has a specific density of about 25
pounds per cubic foot. Lean meat has a specific density greater
than 63 pounds per cubic foot, and fat has a specific density less
than the specific density of lean meat. Therefore, supercritical
carbon dioxide will quite rapidly stratify to the upper level 2512.
Lean meat will stratify by dropping to the lowest level 2530, and
the liquefied fat will tend to remain in the central area 2520.
Pressure vessel 2510 may be fitted with instrumentation for
monitoring or metering any stream into or out of pressure vessel
2510. Instruments may determine fat, lean, and moisture content of
any stream. Immediately prior to the transfer into pressure vessel
2510, the fat content of the stream is measured, and therefore, the
quantity of lean meat can be estimated since the amount of carbon
dioxide can also be measured. The amount of carbon dioxide mixed
with the fat/lean meat stream can likewise be measured and
therefore each stratified item can be extracted from vessel 2510
based on the known mass flow. The liquefied fat can be extracted
via port 2524 in the center of vessel 2510. The carbon dioxide can
be extracted via port 2504 in the upper section of vessel 2510, and
the lean meat can be extracted via port 2532 in the lower section
of vessel 2510. In order to assist in ensuring that only carbon
dioxide is extracted via port 2504, a level measuring device 2502
is arranged to measure the upper level of liquefied fat between the
broken lines shown between arrows 2508 and 2514. A second level
measuring device 2506 is arranged to measure the lower level of
liquefied fat between the broken lines shown between arrows 2526
and 2528. In this way, it can be ensured that carbon dioxide will
be extracted via port 2504, and fat via port 2524, and lean meat
through port 2532. Additionally, agents, including salts,
decontaminating agents, processing aids, and water can be
introduced by any port in any quantity.
[0184] Referring now to FIG. 37, an arrangement of equipment to
process meat, is illustrated. The equipment can be used in the
production of multiple streams of ground meat 2698 having selected
fat content after processing, that can be derived from four streams
of meat 2600, 2602, 2604, and 2606. Each stream of meat 2600, 2602,
2604, and 2606 is pumped by pumps 2616, 2634, 2636, and 2724,
respectively. Meat is contained within enclosed conduits for the
full duration of processing into stream 2698 and a carbon dioxide
atmosphere can be provided to fill or substantially exclude any air
and particularly oxygen within the conduits. A high fat stream 2606
generated by boning processes is transferred along conveyor 2612,
and into positive displacement pump 2724. Air can be extracted and
exchanged with carbon dioxide gas. The moisture and fat content of
the stream 2606 is measured by measuring device 2638. An example of
a suitable measuring device is a GMS Microwave System.
Alternatively, an ultrasonic means of analyzing the fat content of
a continuous stream of ground beef or any boneless meat with fat
and lean, can be arranged as follows: an ultrasonic emitter is
rigidly attached to a first side of a conduit through which a
continuous stream of boneless beef is transferred under controlled
pressure and an ultrasonic collection device is rigidly attached
and a position diametrically opposite the emitter on the same
conduit such that the ultrasonic energy emitted by said first
ultrasonic energy emitter can be collected by said collection
device. In this way the profile of ultrasonic energy emitted by
said ultrasonic sound emitter and transferred directly through the
stream of ground meat within said pressurized conduit can be
compared with the profile of the ultrasonic energy collected by
said collection device and by evaluating the differences between
the sonic input with the sonic output, the fat content can be
determined. The fat content of ground beef can be accurately
measured in this way in a continuous process. The ultrasonic method
of fat analysis described herein above can be substituted for the
GMS method as also described herein and in any other associated
patent disclosures referenced herein. Carbon dioxide is pumped from
conduit 2624, at a pressure above about 1056 psig and temperature
above about 87.degree. F., such that the carbon dioxide is in its
supercritical phase. A crushing device 2726 blends the carbon
dioxide and meat stream 2606 together prior to transferring into
conduit 2640. Conduit 2640 comprises equipment as generally
described in association with FIG. 38 below. After a sufficiently
prolonged exposure of the meat to the supercritical carbon dioxide,
during transfer along conduit 2640, the combined stream is
transferred into pressure vessel 2654, where supercritical carbon
dioxide is extracted via conduit 2650, and after compressing with
compressor 2712, is transferred directly into storage pressure
vessel 2626. Liquefied fat is extracted via conduit 2642. Lean beef
with reduced fat content is transferred along conduit 2660, and
measured with measuring device 2668 so as to determine the fat
content of the meat in conduit 2660. Vessel 2654 can be the vessel
described in association with FIG. 36. The quantity of lean meat
transferred through conduit 2660 into continuous blender 2678 is
controlled in proportion to a second stream from the combined
streams 2600, 2602, 2604. Streams 2600, 2602, 2604 and 2606 are
transferred through conduits into continuous blender 2678 to allow
production of a stream of meat having a fat content as desired
leaving continuous blender 2678.
[0185] Carbon dioxide is stored in vessel 2706. Conduit 2710 allows
vessel 2706 to be filled with carbon dioxide from an exterior
source. Conduit 2715 allows carbon dioxide gas to be transferred
into pressure vessel 2626. Vessel 2722 is arranged with a heater to
raise the temperature of carbon dioxide transferred along conduit
2624, to ensure that carbon dioxide delivered to conduit 2640 is at
supercritical temperature and pressure. An additional carbon
dioxide storage vessel 2720 is replenished by an outside source
transferred from conduit 2632. Compressors 2716 and 2682 recycle
carbon dioxide extracted from equipment 2658 and 2678, and transfer
the carbon dioxide into vessels 2714 and 2720, in readiness for
subsequent use. Conduit 2676 allows the transfer of carbon dioxide
into continuous blender 2678. A supply of carbon dioxide gas is
transferred along conduit 2620, into pumping vessels 2616, 2634,
and 2636. A supply of carbon dioxide is supplied into equipment
2658 along conduit 2652. Pumping vessels 2616, 2634, 2636, and
2724, can be any suitable pump, such as meat pumps manufactured by
Marlen. FIG. 37 shows three streams of boneless meat transferred
along conveyors 2608, 2614, 2610, directly into meat pump vessels
2616, 2634, and 2636, filled with carbon dioxide. Each stream is
pumped along conduits through GMS measuring devices 2646, 2644, and
2648, wherein fat and moisture can be measured prior to transfer
into decontamination apparatus 2658. The mass flow of each stream
is adjusted according to fat content and/or the moisture content to
produce meat of a desired fat and moisture content. The mass flow
of each stream can be adjusted according to its fat content in such
a way that meat with a selected fat content can be transferred into
apparatus 2658. Apparatus 2658 can decontaminate the meat. The
decontaminated meat is transferred along conduit 2670 and through
GMS measuring device 2666 into a continuous blender 2678, to enable
continuous blending with a second stream of meat delivered via
conduit 2660. Continuous blending ensures adequate mixing of the
two streams in the continuous mixer 2678 prior to transfer
therefrom, via measuring device 2722. The stream of blended meat is
transferred into diverter valve 2684 which diverts the stream into
vessels 2690, 2692, 2694, 2696, or 2688 through a distribution
conduit 2680. Carbon dioxide from storage vessel 2706 can be
introduced via conduit 2704 into any one of storage vessels 2690,
2692, 2694, 2696, and 2688. Any meat that does not meet
requirements after measurement by measuring device 2722 can be
transferred along conduit 2686 into vessel 2674, after being
diverted by diverter valve 2684. Such meat not meeting specified
requirements and stored in vessel 2674 can be transferred for
blending at specified rate via measuring device 2672 into
continuous blender 2678.
[0186] Referring now to FIG. 38, a series of conduits for treating
meat with supercritical carbon dioxide, is illustrated. Blending
device 2804 blends meat transferred therein along conduit 2842.
Parallel conduits 2844, 2840, 2838, 2836, and 2800 are connected
together via extraction vessels 2828, 2830, 2814, 2818, and 2810.
Each extraction vessel is fitted with an extraction port to enable
extraction of liquefied fat. Extraction ports 2824, 2848, 2846,
2848, 2820, and 2832, are arranged to allow extraction of the fat.
The apparatus enables a high fat stream of meat to be treated with
supercritical carbon dioxide to produce low fat meat transferred
via conduit 2800. The fat content of the extracted meat stream is
substantially less than the fat content of the stream transferred
into conduit 2842. Blending device 2806 may be located at end of
conduit 2800.
[0187] Referring now to FIG. 39, an apparatus for processing goods,
including meat, is illustrated. The apparatus includes a series of
pressure vessels that can be described as unsealed pressurized
enclosures that hold pressure and allow the continuous transfer of
meat.
[0188] Boneless meat is loaded into vessel 2902. The meat may be
chilled prior to loading therein, to a temperature in the range of
about 28.degree. to about 45.degree. F, but most preferably to a
temperature of about 35.degree. F..+-.10.degree.. The apparatus is
arranged to perform several functions, that include the extraction
of a measured quantity of fat from the meat that is transferred to
vessel 2902. The processed meat can be transferred to a continuous
blender, wherein the continuous blender may be arranged with a
supply of two or more streams of meat.
[0189] The equipment is arranged to periodically and automatically
test for and determine the presence of bacteria. Samples for
testing can be extracted via extraction port 2968. The sample that
is extracted may be a fluid that has accumulated at the base of
vessel 2902. The fluid so removed can contain bacteria from the
meat, and can be representative of the population of bacteria
present within the meat. The extraction point will be arranged such
that the fluid that is extracted is representative of the meat. The
sample extracted can be automatically tested. The automatic testing
apparatus, which is not shown in FIG. 39, is arranged to apply the
samples continuously to a surface of a strip of indicator material.
Samples are in full and intimate contact with the strip of
indicator material for a sufficient and effective period of time
that will result in a color change in the indicator material when
bacteria are detected. The indicator material, is a continuous
strip of engineered polymerized molecular film (hereinafter
"EPMF"). The EPMF strip of material can be transparent so as to
enable light to be projected therethrough, or alternatively
reflected therefrom. After the samples have been in contact with
the surface of EPMF for sufficient time to cause any color change
as a result of the presence of a particular bacteria, the sample
can be removed from the material and a source of light projected
through the strip and onto a light receiver that forms part of a
vision system capable of detecting color changes. Such color
changes can be detected, and the presence of bacteria can be
determined. The information regarding the presence of bacteria or
other recognizable contaminants can be recorded and associated with
the meat, and recorded in a database. The presence of bacteria may
cause a signal or an alarm to sound, enabling the apparatus or
operators to respond accordingly. However, in view of the automated
capability of the apparatus, such meat that is detected to contain
undesirable bacteria, can be directed to a vessel that is not shown
in FIG. 39, but that would store the contaminated meat. The
contaminated meat can subsequently be used for the production of
cooked food products wherein the cooking process will kill any
bacteria that is present. The apparatus described herein for
automatic detection of undesirable bacteria can also be integrated
at the end of the process where the processed meat is ejected, or
alternatively as shown in FIG. 39 at extraction port 2970.
[0190] The process disclosed herein furthermore includes a method
to decontaminate the meat of microorganisms, such as bacteria. A
concentrated solution of sodium chlorite is injected into conduit
2964 in an amount that can be automatically adjusted, by, for
example, the quantity of fat removed from the meat and the water
content of the meat. The sodium chlorite solution is injected via
port 2966. Vessel 2902 is connected directly to a meat pump capable
of pumping at variable speeds to vary the meat flow rate through
conduit 2964, and the pressure can also be controlled. A series of
fat, water, and protein measuring devices, are shown as items 2904,
2948, 2944, 2924, 2936, and 2960. The measuring devices are
integrated into the conduits to enable the automatic measuring of
the meat properties, including, but not exclusively, flow rate,
weight, water content, fat content, and lean meat content. Vessel
2906 is connected through measuring device 2948 and conduit 2966 to
vessel 2946. Vessel 2946 is connected to vessel 2922 via conduit
2916. GMS measuring device 2944 is located on conduit 2916. Vessel
2922 is connected via conduit 2962 and measuring device 2924, to
vessel 2958. Vessel 2958 is connected via conduit 2934 to pumping
vessel 2928, which in turn transfers meat through measuring device
2960 and conduit 2932.
[0191] The meat pumped into vessel 2906 is blended with sodium
chlorite solution injected via port 2966. Vessel 2906 is fitted
with impellers that both mix the sodium chlorite solution and meat
together, while transferring the meat stream into pump 2950. Carbon
dioxide and water can be added to vessel 2906 via port 2954 at a
selected pressure and temperature. The pressure maintained in
vessel 2906 can be greater than or about 500 psig to about 850
psig. As the meat is transferred into vessel 2906, the water
content, fat content, and lean meat content are measured by
measuring device 2966. Pump 2950 transfers the meat and increases
its pressure to about 1100 psig to about 2000 psig. The temperature
at the surfaces of the boneless meat is elevated to greater than
about 90.degree. F. as it is transferred through vessel 2906.
Heating can be by way of a steam jacket installed around vessel
2906, for example. The temperature of the meat can be maintained
above about 90.degree. F. and below about 109.degree. F. Meat
pumped by pump 2950 is transferred through measuring device 2948,
and the mass flow and pressure are controlled as required by a mass
flow regulator installed in conduit 2966. The heated meat is
blended with the sodium chlorite solution in a manner that
substantially ensures that the sodium chlorite solution thoroughly
covers all surfaces of the meat and is forced into crevices, slits,
cuts, and cracks in the meat and fat, in sufficient quantities. The
meat transferred directly into pressure vessel 2946, is blended
with a measured supply of supercritical carbon dioxide injected via
port 2910. The blend of meat, sodium chlorite solution, and
supercritical carbon dioxide, is continuously blended in pressure
vessel 2946. The supercritical carbon dioxide can cause a rapid
lowering of the pH on contact with the sodium chlorite solution at
the surfaces of the meat. The pH can be about 2 to about 3. Under
these conditions, carbonic acid, hypochlorous acid, and
hydrochloric acid are produced at the meat surfaces. The
combination of acids is lethal to pathogens, including E. coli
0157:H7, salmonella, and other pathogens. In addition to
substantially killing the majority of the pathogens and bacteria,
the supercritical carbon dioxide will dissolve fat. Supercritical
carbon dioxide is an effective solvent and will dissolve fats at a
predictable rate. The flow of supercritical carbon dioxide through
port 2910 is controlled according to the fat content and water
content of the meat. The dissolved fat with other contaminants
therein, and a major portion of the sodium chlorite solution, are
extracted via conduit 2914. Vessel 2946 can be arranged in a manner
that enables the separation of the combined stream of materials
flowing through vessel 2946, into two streams, wherein the first
stream includes dissolved fat and is directed through port 2914,
and a second stream includes meat that is transferred through mass
flow regulator fitted in conduit 2916, and through measuring device
2948. The fat, water, and lean meat content of the meat stream are
measured with measuring device 2948, before exposure to
supercritical carbon dioxide in vessel 2946, and then again with
measuring device 2944, after treatment in vessel 2946. The
difference in fat, water, and lean meat content can be calculated.
The information can be used to control the mass flow and pressure
of the carbon dioxide and water provided to pressure vessel 2946.
Most particularly, the fat and water content of the meat can be
adjusted while substantially killing and removing surface pathogens
and other contaminants. The treated meat is transferred through
measuring device 2944 into vessel 2922, wherein a pressure drop
from the specified gas pressure within vessel 2946 occurs. The
pressure can drop from the higher level of about 1100 psig to about
2000 psig, to a lower pressure of about 500 psig to about 750 psig.
Such a pressure drop will cause a rapid reduction in the meat
surface temperature and pH. Vessel 2922 is therefore controlled at
an internal pressure of about 500 psig to about 750 psig. The
temperature of the meat can also be adjusted within vessel 2922 by
injection of liquid or dense carbon dioxide gas via port 2940, and
carbon dioxide gas can be extracted and recycled, via conduit 2920.
If so desired, a pathogen and/or bacteria detection system, as
described hereinabove, may be installed between vessel 2922 and
vessel 2958. The treated meat is regulated from vessel 2922 through
conduit 2962. The meat is then transferred through measuring device
2924 and into vessel 2958, which is substantially similar to vessel
2922, having port 2938 for the addition of carbon dioxide. Gas is
extracted from vessel 2958 via port 2956. The temperature and
pressure of the meat are measured at selected points. Adjustments
can be automated and executed by a computer. Data or measurements
can be recorded and associated with the meat as it is transferred
through the vessels so that the meat from different animals remains
associated with the data pertaining to the animal and tracked
throughout the process. The method for identification of the meat
with an animal is enabled by controlling mass flow, and with
volumetric measurement, the location of any identifiable portion of
meat can be tracked to the animal. The data collected can be
recorded in a database, wherein said database is accessible by
multiple users. The meat's properties, including its origin, age,
and all other properties, can be associated with any package
containing the meat and a label containing any information can be
attached to the package.
[0192] The meat is then transferred from vessel 2958, through
conduit 2972, through measuring device 2936, followed by transfer
through conduit 2934, and into vessel 2928. A pump enables pumping
of the treated meat through measuring device 2960, and into conduit
2932. Conduit 2932 can be attached directly to an enclosed storage
vessel (not shown), which is temperature controlled, and filled
with a selected gas, enabling storage of the processed meat in
readiness for subsequent processing or packaging.
[0193] A pressure drop between vessel 2922 and vessel 2958, can
occur to lower the pressure in the range of about 50 psig to about
atmospheric pressure. Such lowering of pressure will result in a
temperature drop. Port 2938, for example, may provide a gas, such
as carbon dioxide, at a temperature that enables adjustment of the
temperature of the meat. Such temperature adjustment may require
elevation or reduction according to the original temperature of the
boneless meat provided into vessel 2902.
[0194] The sodium chlorite solution applied to the surfaces of
boneless meat in vessel 2902 may be applied, in concentrations from
500 ppm to 1200 ppm according to USDA regulation 21 C.F.R. .sctn.
173.325. However, given the effective removal of a substantial
proportion of the added sodium chlorite solution with the liquefied
fat extracted from vessel 2946, it is anticipated that higher
concentrations of the sodium chlorite solution may be used. For
example, a concentration above 1,200 ppm, such as about 2,500 ppm
to about 3,000 ppm and above, should be possible according to the
invention.
[0195] The increased quantities of sodium chlorite will enable
application of increased quantities of water, resulting in
significantly improved antimicrobial effects.
[0196] In one embodiment of the invention, after application of a
sodium chlorite solution of concentration from 500 ppm to 1200 ppm
in accordance with USDA regulation 21 C.F.R. .sctn. 173.325 in
vessels 2902 and 2906, the removal of substantially all sodium
chlorite solution (including excess water) during processing in
vessel 2946 is possible. Therefore, a second application of sodium
chlorite solution, at a selected and automatically adjusted
concentration, can be injected at a controlled mass flow rate via
port 2940 in vessel 2922. Carbon dioxide gas at about 550 psig and
water can be introduced via another port, such as a bottom port in
the lower sections of vessel 2922. The carbon dioxide addition can
be combined with a heating system to elevate the temperature of
carbon dioxide to a temperature of about 90.degree. F. to about
109.degree. F. Carbonic acid is produced having a pH of about 2 to
about 3. The treatment according to the invention ensures that the
pathogen population is reduced to an undetectable level.
[0197] Sodium chlorite solution with water and carbon dioxide can
be extracted via port 2920. The fat and sodium compound(s) with
excess water can be extracted via port 2932. Excess water is
removed, in part, by entrainment with the carbon dioxide gas when
vented.
[0198] The extracted liquid fat can then be separated from the
sodium compound solution removed therewith by centrifuge or a
separation column. Fat can then be pasteurized by elevating the
temperature to a range of about 140.degree. to about 160.degree.
F., filtered, and processed, such as by freeze-drying.
[0199] The apparatus can enable the application of high
concentrations of sodium chlorite solution mixed with the meat to
ensure adequate contact and saturated coverage of all exposed
surfaces of meat, followed by adequate concentrations of carbonic
acid solution at a pH of about 2 to about 3, thereby enabling
reduction of pathogens to an undetectable pathogen population in
the finished boneless meat.
[0200] Another aspect of the invention relates to a method and
apparatus for processing meat by providing at least two input
streams of ground meat to a mixer, controlling the mass flow of
each stream, measuring at least the fat content of each stream, and
combining the streams into a single output stream and measuring the
fat content of the combined stream; adjusting the mass flow of the
input streams to produce blended ground meat with a selected
proportion of fat, lean, and water. The present invention can
provide for the detection of measurement readings that have drifted
from actual, and the manipulation of measurement readings to
provide more accurate control of the controlled variable in meat,
whether it is fat, lean, or water.
[0201] The methods and apparatus use measuring devices that may
require periodic calibration. Such calibration has hitherto
required an intervention procedure resulting in lost production
time and the need to occasionally reprocess "out of specification"
ground meat that has been produced with defective measuring devices
that have not been correctly calibrated.
[0202] The present invention provides a method of operation and an
automated process to enable calibration of measuring devices used
in the automatic production of ground meat.
[0203] According to one embodiment of the invention, a method of
controlling the rate of a pump for an input stream to a mixer
having a plurality of input streams being mixed into an output
stream is provided. The method includes obtaining a plurality of
composition measurements of an input meat stream being transferred
by a pump. The method includes calculating a representative
measurement based on the plurality of measurements. The method
includes determining the flow rate capacity of the pump based on a
controllable pump factor. The pump factor can include the speed.
The method includes calculating the controllable pump factor that
is calculated to give an input meat flow rate that will provide a
meat product within a composition range and a flow rate range,
wherein the meat product is comprised from at least two input meat
streams of different compositions. The input meat flow rate is
obtained by solving a mass balance equation around the mixer using
the representative measurement to solve for the input meat flow
rate.
[0204] According to another embodiment of the invention, a method
of selecting one measurement reading from a pair of measurement
readings, to use as a measured variable in the control of an input
stream to a mixer having a plurality of input streams being mixed
into an outlet stream, is provided. The method includes obtaining
the composition measurement readings from input streams and the
output stream around the mixer. The method includes calculating
obtaining the flow rates of input streams and the output stream
around the mixer. The method includes calculating a predicted input
stream composition by solving a mass balance equation around the
mixer using the flow rates and the composition measurement
readings, but for the one composition being solved. The method
includes calculating the difference between the predicted input
stream composition and the composition measurement reading from a
measuring device from the same input stream. The method includes
selecting the measurement reading from a redundant measuring device
for use as the measured variable when the absolute value of the
difference is outside of a threshold.
[0205] According to one embodiment of the invention, a method of
detecting inaccuracy in a measuring device of an input stream to a
mixer having a plurality of input streams being mixed into an
output stream is provided. The method includes obtaining
composition measurement readings from input streams and an output
stream around the mixer. The method includes obtaining the flow
rates of input streams and the output stream. The method includes
calculating a predicted input stream composition by solving a mass
balance equation around the mixer using the flow rates of the
composition measurement readings, but for the one composition being
solved. The method includes calculating the difference between the
predicted input stream composition and the composition measurement
reading from a measuring device from the same input stream. The
method includes determining if the measuring device is inaccurate
when the absolute value of the difference is outside of a
threshold.
[0206] According to one embodiment of the invention, a method of
calibrating a first measuring device from a second measuring device
on an input stream to a mixer having a plurality of input streams
being mixed into an output stream, is provided. The method includes
obtaining composition measurement readings from input streams and
an output stream around the mixer. The method includes obtaining
the flow rates of input streams and the output stream around the
mixer. The method includes calculating a predicted input stream
composition by solving a mass balance equation around the mixer
using the flow rates and the composition measurement readings, but
for the one composition being solved. The method includes
calculating the difference between the predicted input stream's
composition and the composition measurement reading from a
measuring device from the same input stream, and assigning the
measurement reading from the second measuring device to the first
measuring device when the absolute value of the difference is
outside of a threshold.
[0207] In all the above alternative embodiments, measurement
readings can be taken from all input streams and output streams. In
all the above embodiments, the flow rates of input and output
streams can be determined from a controllable pump factor or by
measuring. Alternatively, some input streams will have a known and
substantially unvarying composition. Also, their flow rate can be
substantially unvarying. These known factors can still be used in
solving the mass balance equation. However, due to their unvarying
composition and flow rate, the composition need not be measured nor
their flow rate determined.
[0208] The methods and procedures disclosed herein enable automated
calibration of each measuring device during the normal operation of
the apparatus, when measuring the content of each stream.
[0209] Automated production of ground meat, having a specified
amount of fat, lean, and water content in any desired ratio, is
enabled by combining at least two input streams of ground meat,
pumped through conduits by variable-speed pumps, and mixed together
to provide one output stream having the controlled variable within
a specified range. The output stream can be produced within a
specified flow rate range. The pumps are capable of adjusting the
mass flow of each input stream to achieve an output stream within a
specified composition and flow rate range. The mass flow of each
input stream is adjusted according to the measured fat, lean,
and/or water content of each input stream so that, when the streams
are combined into a single output stream, the resultant fat, lean,
or water ratio in the combined output stream is controlled within
the specified range. The pumps are monitored for flow rate in an
effort to maintain the output stream within a specified flow rate
range. Pumps can be constrained from exceeding the upper limit of
the output stream's flow rate. Pumps can also be constrained from
dropping the output stream's rate below the lower limit of the
output stream's flow rate range. It is not entirely necessary to
maintain the input streams at any specified constant ratio prior to
mixing the streams together. The variable that is desired to be
controlled in the output stream may be allowed to vary in the input
streams because the measuring devices measuring the input stream's
composition immediately downstream of the pumps will adjust the
flow rate of each input stream in the correct proportions to
produce a mixed output stream having a controlled amount of fat,
lean, or water, in any desired range. Measuring devices are
installed in each of the input streams and also in the combined
output stream. Mass flow adjustment of each stream is controlled by
a computer that processes data received from each measuring device,
and then directs adjustment of each pump's speed independently,
according to the measured content of each stream, so as to produce
an output stream of specified ground meat. The processing of data
from the measuring devices in the manner described herein is useful
to control the input stream meat pumps, or in detecting drift seen
in some measuring devices, or in selecting one from a pair of
measuring devices. The method for automated ground meat production,
according to the invention, has been found to be a significant
improvement compared with other production methods. However the
accuracy of the streams' content measurement reading is affected by
a gradual divergence from a calibrated setting and recalibration
may be required periodically. In one embodiment, the present
invention provides a method for detecting when a measurement
reading has drifted, and selecting an alternative reading. Drift
when used in the context of measuring devices refers to deviation
of measurement readings from the true reading, which may occur
gradually.
[0210] Referring to FIG. 40, one embodiment of an apparatus is
illustrated for the processing of goods, including boneless beef,
or boneless meat of any kind, including pork, poultry, and any
other protein containing fat, wherein the meat is derived from an
animal source, and the fat, lean meat, and water content is unknown
after harvesting from the animal's skeleton. The apparatus includes
a series of pressure vessels that may be described as unsealed
pressurized enclosures arranged to process two streams of meat.
However, it should be appreciated that other embodiments may have
more than two input streams. Some embodiments may have more than
one output stream, and other embodiments may have one or more
recycle streams. In other embodiments, additives can be provided to
the input streams, including spices, particularly for sausages. "An
unsealed pressurized enclosure" refers, in part, to the vessels'
ability to process the meat in a continuous mode under positive
pressure (at least from grinder to end of mixer). In one
embodiment, the apparatus includes two input streams for processing
beef from a grinder to a mixer to form a single output stream. The
apparatus associated with each stream includes at least a grinder,
a preblender (which mixes an input stream), a pump, and connecting
conduits. Measuring devices may be located between grinder and
preblender, and after the pump. The grinders, preblenders, pumps,
and mixer can be provided by the Wenger Company. The apparatus is
capable of grinding the separate streams of boneless meat,
measuring the fat, lean, and water content of each stream, and
adjusting the flow of each input stream according to a measured
variable content of the respective streams. The two streams are
combined together to form a single output stream, which is also
measured to confirm the combined content of fat, lean, and water
therein.
[0211] In one embodiment, two separate quantities of boneless meat
with differing quantities of fat, lean, or water, are loaded into
loaders 3402 and 3426. Boneless meat, such as beef, may be chilled
prior to loading, to a temperature in the range of about 28.degree.
to about 45.degree. F., but most preferably to a temperature of
about 35.degree. F..+-.1.degree. F.
[0212] The second stream of boneless meat represented by arrow 3428
is processed in much the same manner as is the first stream of
boneless meat represented by arrow 3400.
[0213] The first stream of boneless meat is loaded into a
variable-speed meat grinder 3406 by loader 3402 and conveyor 3404,
which may be fitted with a metal detector. Grinder 3406 is driven
most preferably by a variable-speed motor, which may be a hydraulic
motor, and in such a manner that will enable a continuous flow of
meat to be ground at a mass flow that can be varied as required to
adjust to the demands of the system and, more particularly, the
proportioned flow into continuous blender 3414. For example,
grinder 3406 may have level-indicating devices that monitor the
levels in the meat grinder vessel and the grinder can be sped up or
slowed down to maintain the level within a suitable range. Grinder
3406 is arranged to transfer ground meat along an enclosed conduit
3472 through measuring device 3408 and into preblender 3412.
Grinder 3406 can be covered, apart from an open section to allow
meat to drop into the hopper. The measuring device 3408 can measure
the fat, lean, and water content in the first stream of meat.
Preblender vessel 3412 receives product pumped therein, and blends
the stream of ground meat while transferring said meat to the
continuous mixer 3414. The preblender vessel 3412 is fitted with
impellers mounted internally that are arranged to blend meat
transferred therein and also to carry it toward the continuous
mixer 3414. The impellers mounted in preblender vessel 3412 may be
arranged with any suitable profile including paddles and Archimedes
screw sections to enable efficient blending and removal of gas that
may otherwise become entrapped within the meat stream as it is
transferred into conduit 3470 by pump 3484. The meat pump 3484 can
be a positive displacement piston-type pump, vane pump, or screw
pump that may be a matching twin screw or single screw, having a
parallel or conical profile, to increase pressure. The preblender
vessel 3412 can also be provided with level indicators that will
indicate the level of the meat in the vessel. If the level
indicators indicate a high level, the grinder 3406 may be slowed
down or temporarily stopped. Alternatively, the pump 3484 may be
sped up to decrease the level in the preblender.
[0214] The type of pump 3484 may be selected from any number of
pumps and may comprise, for example, a pair of counter- or
corotating, meshed, conical screws arranged to compress the stream
of meat and diminish any gas voids contained within the meat
stream. Such gas inclusions can comprise a large proportion of
carbon dioxide, which can dissolve into the water and oils
contained in the meat when suitably compressed. Preblender vessel
3412 is also fitted with an exhaust duct 3484 so as to allow
extraction of gases, such as carbon dioxide, that can be injected
into vessel 3412 through bottom injectors, which can also enable
the adjustment of the temperature of the meat blended therein. Gas
supply source 3430 will supply liquid carbon dioxide to vessels
3412 and 3406. Carbon dioxide liquid will vaporize immediately
after release by control valves, which can be used to control the
temperature. Exhaust duct 3434 for vessel 3412 can be fitted with
an extractor fan or may have a butterfly valve to maintain or
control a selected pressure in the vessel. Exhaust duct 3434 will
thusly carry any vaporized amount of water and can be used to
control the water content in the meat stream.
[0215] From pump 3484, meat is transferred through conduit 3470
with measuring devices 3438 and 3440 conveniently mounted therein,
and into the continuous blender 3414. Continuous blender 3414 is a
mixer to mix the first and second input streams.
[0216] The second stream of boneless meat is loaded into a
variable-speed meat grinder 3422 by loader 3426 and conveyor 3424,
which may be fitted with a metal detector. Grinder 3422 is driven
most preferably by a variable-speed motor that may be a hydraulic
motor and in such a manner that will enable a continuous flow of
meat to be ground at a mass flow that can be varied as required to
adjust to the demands of the system and, more particularly, the
proportioned flow into continuous blender 3414. For example,
grinder 3422 may have level-indicating devices that monitor the
levels in the meat grinder vessel and the grinder can be sped up or
slowed down to maintain the level within a suitable range. Grinder
3422 is arranged to transfer ground meat along enclosed conduit
3474 through measuring device 3420 and into preblender 3416.
Grinder 3422 can be covered, apart from an open section to allow
meat to drop into the hopper. The measuring device 3420 can measure
the fat, lean, and water content in the second stream of meat.
Preblender vessel 3416 receives product pumped therein, and blends
the stream of ground meat while transferring said meat to the
continuous mixer 3414. The preblender vessel 3416 is fitted with
impellers mounted internally that are arranged to blend meat
transferred therein and also carry it toward the continuous mixer
3414. The impellers mounted in preblender vessel 3416 may be
arranged with any suitable profile including paddles and Archimedes
screw sections to enable efficient blending and removal of gas that
may otherwise become enclosed within the meat stream as it is
transferred into conduit 3471 by pump 3486. The meat pump 3486 can
be a positive displacement piston-type pump, vane pump, or screw
pump, which may be a matching twin screw or single screw having a
parallel or conical profile to increase pressure. The preblender
vessel 3416 can also be provided with level indicators that will
indicate the level of the meat in the vessel. If the level
indicators indicate a high level, the grinder 3422 may be slowed
down or temporarily stopped. Alternatively, the pump 3486 may be
sped up to decrease the level in the preblender.
[0217] The type of pump 3486 may be selected from any number of
pumps and may comprise, for example, a pair of counter- or
corotating, meshed, conical screws arranged to compress the stream
of meat and diminish any gas voids contained within the meat
stream. Such gas inclusions can comprise a large proportion of
carbon dioxide that can dissolve into the water and oils contained
in the meat when suitably compressed. Preblender vessel 3416 is
also fitted with an exhaust duct 3452 so as to allow extraction of
gases, such as carbon dioxide, that can be injected into vessel
3416 through bottom injectors, which can also enable the adjustment
of the temperature of the meat blended therein. Gas supply source
3456 can supply liquid carbon dioxide to vessels 3416 and 3422.
Carbon dioxide liquid will vaporize immediately after opening of
control valves to control the temperature. Exhaust duct 3452 for
vessel 3416 can be fitted with an extractor fan or may have a
butterfly valve to maintain or control the pressure in the vessel.
Exhaust duct 3452 will thusly carry any vaporized amount of water
and can be used to control the water content in the meat stream.
Gas supplies 3430 and 3456 are fed to grinders 3406 and 3422 and
preblenders 3412 and 3416 to displace air and oxygen.
[0218] From pump 3486, meat is transferred through conduit 3471
with measuring devices 3446 and 3448 conveniently mounted therein,
and into the continuous blender 3414. Continuous blender 3414 is a
mixer to mix the input streams. Continuous blender 3414 is
preferably controlled within a specified flow rate range.
Accordingly, the control of pumps 3470 and 3471 may be arranged to
cooperatively produce a combined flow rate that will neither exceed
the upper limit of the range nor drop the flow rate below the lower
limit of the range. For example, one pump can be selected as the
master of the combined flow controller; however, if the pump were
to reach its operating limit, the slave or second pump may be
engaged in combined flow control mode. Pumps will typically operate
in composition control mode, but flow will be monitored and
controlled as well. Operation of the pumps may result in
constraining the pump speed not to increase or decrease if it would
result in the combined output stream being outside the combined
output composition range. Back pressure in conduits 3470 and 3471
is created by controlling the flow of combined streams through the
continuous blender 3414.
[0219] Each stream of boneless beef that has been ground is
preferably fed into preblenders 3412 and 3416. Blending each stream
in isolation, prior to combining with another stream, can provide a
substantially homogenous stream of meat that can decrease the
variation in measurements taken by measuring devices 3438, 3440,
3446, and 3448, respectively. The pressure in the preblenders can
be elevated by controlled restriction of the exhaust, which will
prevent ingress of atmospheric oxygen.
[0220] The equipment is arranged to automatically measure at least
one component of each stream of meat coming into the continuous
blender. The measured component may be fat, lean, and water or any
other component or characteristic of the meat. The measurements are
made as the streams are transferred through measuring devices 3438,
3440, 3446, and 3448, installed after pumps 3484 and 3486,
measuring devices 3408 and 3420 installed after grinders 3406 and
3422, and measuring devices 3478 and 3460 installed after the
continuous mixer. The measuring devices can be GMS and/or AVS
devices. The measuring devices, which are preferably of the GMS
type, are integrated into the conduits to enable automatic
measuring of the meat properties, which may include but are not
limited to, weight, water content, fat content, and lean content,
thereby enabling the automatic adjustment of the pumps 3484 and
3486.
[0221] Additionally, all vessels, equipment, and connecting
conduits can be filled with selected gases as required. The gas may
comprise at least carbon dioxide or nitrogen. But in any event, the
gas should have reduced amounts of oxygen in proportions lower than
normal air. The continuous blender 3414 is driven by a
variable-speed motor, thereby combining first and second streams
into a single stream that is transferred through blender 3414 and
mixed therein by screws enclosed therein. The combined and blended
stream of meat can be transferred through conduit 3458 and through
measuring devices 3478 and 3460. Conduit 3458 is connected to
hopper 3462 with an optional positive displacement pump 3476 at one
outlet. It should be noted that the continuous blender 3414 has
adequate capacity to pump the combined streams and a fine grinder
could be mounted directly to the exit end of the continuous blender
if so desired. Pump 3476, optionally can be provided with a grinder
to finely grind meat. Hopper 3462 can be arranged with a conical
profiled side elevation and can be fitted with a mixer mounted
therein. The variable-speed, positive-displacement pump 3476 is
connected directly to the base of the conical profiled hopper 3462
so as to enable a controlled pumping of the stream of meat into
conduit 3464. Conduit 3464 may be arranged with an outer jacket in
a manner to allow heated water to pass therethrough, enabling the
heating of the conduit 3464. Such heating can minimize the buildup
of fat on the internal walls of the conduit 3464, which may
otherwise accumulate excessively.
[0222] In one embodiment, conduit 3464 is connected to a chub
packaging apparatus 3466 with a chub clipping and transfer section.
Filled, clipped, and sealed, substantially oxygen-free chubs, which
may also be evacuated, are then transferred onto conveyor 3468.
Conveyor 3468 is arranged to transfer finished chub packages into a
refrigerated storage room and labeling station, and/or further
packaged into cartons that can then be loaded onto pallets in
readiness for shipping. Chub packages can be labeled or marked with
an identification mark that is associated with all types of
information that can be retrieved via a computer.
[0223] Continuous blender 3414 may be provided with an enclosed
screw-style transfer and blender driven by a variable-speed driver.
Alternative mixing devices can be integrated into the automated
ground meat production system, as herein described. For example,
grinders 3406 and 3422 may be used to blend the combined first and
second streams of meat.
[0224] Measuring devices 3408, 3420, 3438, 3440, 3446, 3448, 3478,
and 3460 may be used to measure the fat, water, and/or lean content
of meat streams transferred therethrough. However, when GMS
measuring devices are installed in close proximity to each other,
the operation of each device, when taking a measurement reading,
should be staggered so that only a single device is actively
measuring at any one time. The GMS devices utilize microwave (radio
frequency) and interference can occur between the devices when
operated at the same time. Staggering the operation of the devices
may avoid interference. The GMS devices are capable of actively
measuring at a rate of approximately 1-2 times per second. For
example, device 3408 may be activated to read a first measurement
followed in sequence by device 3438, then 3440, 3420, 3448, 3446,
3478, and 2460. Following the completion of such a sequence of
measurements, the sequence can be repeated for any number of
cycles. However, it should be appreciated that the order of
measurements may be altered in any manner. In one embodiment, every
measurement reading from one device is added and divided by the
number of readings taken from the device to arrive at an average
reading. Other embodiments may obtain the median reading of all the
measurement readings. Both the average and median readings are
representative readings from a sampling of the readings taken from
one measuring device. It is also possible to have more than one
measuring device at one stream, i.e., pairs of measuring devices or
redundant measuring devices. The readings from one or from all
measuring devices on one stream can be used to obtain an average
measurement or a median measurement. The representative reading
obtained from a plurality of readings is used in computations to
control the apparatus, as further described below. Additionally, it
should be noted that the measurements are taken while each stream
of meat is in motion. The average quantity of meat measured can
vary according to the mass flow of each stream. Therefore, it is
preferable to vary the sequence of measurements for every cycle
and, preferably, a random order can be performed from a virtually
infinite combination of sequences.
[0225] During each sequence or series of measurements, the data
from each measuring device is recorded in isolation from other
device measurements. In this way, a progressive history of
measurements can be recorded in a computer. The computer can
include a database structure stored in memory. The memory can
comprise a RAM component and also a storage hard drive component.
In this way, any number of selected measurements from any
particular measuring device can be accumulated and a representative
measurement is calculated for each measuring device. The
representative measurement can be an average or median, or any
other measure derived from a sampling of readings that is
representative. In one embodiment, for example, the sum of three
consecutive measurements from any one measuring device can be
selected and averaged to yield the average of the three consecutive
measurements. In other embodiments, the measurements of pairs of
measuring devices are added and divided by the number of
measurements taken from both instruments. The representative
measurement, from the subject measuring device or devices, having
measured one particular stream of meat, can then be used in the
computations for the adjustment of the pump associated with the
stream with improved accuracy. Similarly, selected consecutive
measurements from any and all measuring devices can be stored, and
processed to provide representative measurements that can then be
used to adjust the flow of the associated stream with pumps.
Furthermore, the sum of any number of consecutive measurements can
be averaged, over time, to provide such measurements for mass flow
control of each stream. Alternating measurements from two or more
measuring devices according to any pattern, random or otherwise,
can be accumulated, and averaged to achieve an improved performance
of the automated apparatus for ground meat production. Any trends
that may be caused by measuring device malfunction or meat
variations can be identified and adjusted as needed without the
intervention of an apparatus operator, according to the invention.
Examples of recorded measurement data manipulation, for the purpose
of improving ground meat production efficiency, can involve
programming of the computer to perform numerous simultaneous
calculations so as to optimize use of the recorded measurement data
that, for example, can include the continuous calibration or
adjustment of the measuring devices.
[0226] In practice, accumulating data from several consecutive
measurements, followed by an averaging of the accumulated
measurements is a preferred method to achieve an improved
homogenized blend of ground meat. The data can also be used to
check and then calibrate or adjust the paired devices, determine
when a device has drifted, select an alternate device, and control
the mass flow of the pumps based on the correctly functioning
device. In FIG. 40, a preferred embodiment shows a total of eight
measuring devices integrated into a production apparatus wherein
two input streams of ground meat are transferred to a mixer and
combined into a single output stream. For the purposes of
facilitating an explanation of the operation of the apparatus, each
measuring device can be assigned a letter. Each input and output
stream will also have a flow rate associated with it. The input
streams are combined to produce the output stream that is
discharged from the mixer 3414. In the first stream, a measuring
device is located in conduit 3472. Conduit 3472 is connected
directly to the pre-blender 3412 with the measuring device D
located therein. Thereafter, the first stream is transferred
through conduit 3470 with consecutively positioned measuring
devices A and a. The first stream terminates when it is combined
with the second stream in the mixer 3414. The second stream is
transferred via conduit 3474, through measuring device E, into
preblender 3416 and then through conduit 3471 with measuring
devices B and b located therein. After transferring input streams
3800 and 3428 to mixer 3414, the combined output stream is measured
again by devices C and c. By conservation of mass, the mass of
input streams will equal the mass of the output stream, allowing
for time for the input streams to arrive at the output stream.
Assuming all measuring devices are operating accurately and reading
the mass fraction of one component, the measurements of one
component passing through devices A and B should be equal to C,
allowing for sufficient time for the mass leaving devices A and B
to arrive at location C. Therefore, this simple mass balance
calculation can be used to check the accuracy and drift of the
measuring devices. Assuming that measuring devices measure a mass
fraction of a component, the need to obtain the mass flow rates
arises. Flow rates can be measured by instrument or assumed from
the pump speed. In some embodiments, pumps may pump a certain
volumetric flow rate for every rotation of the pump impeller taking
into account only slippage. This correlation can, many times be
provided by the pump vendor, or can be determined through simple
experimentation. The speed, as measured by revolutions per minute,
or any other factor that is directly controllable can be correlated
to a volumetric or mass flow rate by including density, passing
through the pump. Additionally, the accuracy of a measurement
recorded by device A can be checked after allowing time for
transfer of the measured stream section to device C by subtracting
the value of a measurement made by device B. Equations can be
solved for every device A, a, B, b, C, c, D, and E. Patterns and
trends can be recognized when measurements are noticed to be
drifting when all other measurements are remaining steady, or
nearly so. A sequence of measurements followed by a series of
calculations can be performed by a computer processor to check the
accuracy of each measuring device by solving mass balance equations
using the measurement readings and the flow rates for every one of
the input streams and the output stream except for the quantity
that is being solved. The solution to a mass balance equation is
the predicted value of what the measurement reading from the
measuring device should be. If the absolute value of the difference
between the predicted measurement and the actual or representative
measurement from the measuring device is greater than a
predetermined limit, the measuring device can be determined to be
inaccurate. This is, of course, after verifying that all other
measuring devices are reading within acceptable limits. If there is
more than one measuring device on any one stream, the measuring
device that has drifted can be calibrated by assigning the value of
the accurate measuring device to the inaccurate measuring device.
In this manner, the measuring device that has drifted, or become
inaccurate, can be recalibrated. In other embodiments, the
measuring device determined to have drifted will be put out of
service, and its redundant pair, or alternate, will be used in
controlling the pump. In other embodiments, the measuring device
with the least amount of error will be the one selected from which
to control the pump. It will also be appreciated that it is not
necessary to incorporate the number of devices as are shown to
achieve the accuracy needed during normal operation of the
apparatus. However if each pair of devices is reduced to a single
measuring device, the malfunction of any single device would most
probably require the apparatus to be shut down to enable
replacement of the malfunctioning device. Such a shutdown and
device replacement can be delayed to a convenient time when
redundant devices or pairs are installed in adjacent locations.
[0227] Referring again to the devices shown as A, a, B, b, C, and
c, other calculations can be programmed into the computer
processor. For example, in addition to the calculation of A+B=C,
the following equations can be used to check accuracy and
performance of any individual device, wherein any letter represents
a mass quantity, calculated by multiplying mass fraction with mass
flow or by any other determination.
C-A=B
C-B=A
a+b=c
[(A+a)+(B+b)]/2=C
C-(A+a)/2=(B+b)/2
A=a
B=b
C=c
(C+c)/2=A+B
a.sub.1=c.sub.1-b.sub.1; b.sub.1=c.sub.1-a.sub.1;
c.sub.1=a.sub.1+b.sub.1
a.sub.2=c.sub.2-b.sub.2; b.sub.2=c.sub.2-a.sub.2;
c.sub.2=a.sub.2+b.sub.2
a.sub.3=c.sub.3-b.sub.3; b.sub.3=c.sub.3-a.sub.3;
c.sub.3=a.sub.3+b.sub.3
[0228] In the event that any particular device is found to
malfunction, it can be recalibrated, meaning that, if a measuring
device is determined to be reading inaccurately, the signal by the
malfunctioning device, is set to equal the measurement of the
properly functioning device. Alternatively, the malfunctioning
device can be excluded from subsequent calculations until it can be
replaced or repaired, and the functioning device can be selected to
take its place.
[0229] Any of the vessels disclosed herein for treatment requiring
the addition of carbon dioxide can be arranged in any suitable
disposition, horizontal, vertical, or inclined to enable, in
particular, the efficient separation of any agent, but most notably
liquid or very dense carbon dioxide, and which may include a
measured/determined quantity of added water, and meat. For example,
it may be more suitable to treat the meat in a horizontally
disposed vessel with paddles therein, and then extract the treated
meat from the horizontal vessel, after any suitable treatment with
any selected agent, with a vertically or inclined screw, such that
the meat has gaps between the pieces allowing the agent, such as
liquid carbon dioxide, to remain in the lower portion of the
vessel. In this way, the liquid or dense gas carbon dioxide can be
substantially removed from the meat prior to any compression of the
meat.
[0230] It is believed that the composition of bacteria cell walls
(at least with respect to the cell walls of the pathogens E. coli
0157-H7, salmonella, and listeria monocytogenes) is a complex
arrangement of lipids (fats). Given that liquid carbon dioxide,
such as supercritical carbon dioxide, is a powerful solvent and
will dissolve fats very aggressively, it may be that the carbon
dioxide dissolves the bacteria cell walls thereby, selectively,
killing these pathogens and dissolving fat, such as in the meat, at
the same time. The dissolution of lipids in cell walls can occur
very rapidly, and can enable the size of the treatment vessel to be
greatly reduced when compared to a vessel relying only upon
lowering of the pH of the carbonic acid to kill the bacteria.
[0231] According to one embodiment of the invention, the goods,
such as meat, can be treated in a first chamber with liquid carbon
dioxide at a temperature above the freezing point of water, such as
in the range of about 34 to about 40.degree. F., and at a pressure
of about 500 psig to about 750 psig, or greater. Liquid carbon
dioxide can liquefy fat which can be extracted therewith. The
goods, such as meat, are treated in a second chamber wherein a
measured amount of water is added with additional carbon dioxide to
produce carbon acid having a pH of about 2 to about 3. Thereafter,
the meat can be further processed, such as by grinding. Grinding
meat greatly increases the amount of surface area, and therefore it
is more effective to treat the meat prior to any substantial
increase in the surface area.
[0232] The water added to the meat must not exceed an amount equal
to the lost water plus less than 0.5% to avoid labeling retail
packaged meat with the amount of added water (to the nearest whole
number), or alternatively if the amount of added water exceeds the
lost water (which has been lost due to evaporation and/or
sublimation of frozen, natural water/ice content of the meat) by an
amount greater than 0.5%, and less than 1%, a retail package
containing the meat must be labeled with the words "1% added water"
and so on.
[0233] Referring now to FIG. 41 a diagrammatic representation of a
cross section through an apparatus is shown wherein processing and
grinding meat in meat grinder 148 followed by blending the stream
of ground meat in space 146 of pressurized vessel 143 with any
suitable fluid such as carbon dioxide. The suitable fluid, such as
carbon dioxide, is transferred in directions such as are shown by
arrows 136 and 154 into space 146 via any suitable number of
conduits such as 142 and 156. The streams of carbon dioxide are
transferred into space 146 via said conduits at a selected and
suitable pressure and mass flow rate under controlled positive
displacement by any suitable positive displacement pump or
plurality of pumps. The combined, blended stream of ground meat and
fluid carbon dioxide is then transferred along conduit 130 at a
controlled pressure and rate of mass flow into the enclosed space
defined by the conduit 186. Said defined space 186 comprises a
space enclosed by a conduit manufactured from any suitable material
such as stainless steel having a round cross section with enclosed
ends defined by at least one cone shaped section which in turn is
connected directly to a smaller diameter section of conduit such as
195. At ends of the conduit 186 conduits are connected directly
thereto which in turn are connected to further series of conduits
through which ground meat and carbon dioxide are transferred after
processing and separating within the space defined by conduit 186.
The single stream of ground meat mixed with a controlled and
adjustable proportion of liquid carbon dioxide, after transfer
along conduit 130 into the space defined by conduit 186, is
separated into two, three or more separate layers. Most preferably
the carbon dioxide fluid will be controlled to any suitable
pressure and most preferably at about 480 psig such that the
specific density of said carbon dioxide is less than the specific
density of the lean meat portion and greater than the specific
density of the fat portion of the ground meat blended therewith.
The conduit 186 is rotated by any suitable variable speed motor
such as an electric or hydraulic motor which is attached thereto in
such a manner that enables the rotating of conduit 186 at a
controlled speed (revolutions per minute) such as at 500 rpm, 1000
rpm, 300 rpm or more or less but most preferably at such a speed
(rpm) that will cause an artificial gravitation to be applied to
the fluid and ground meat transferred into conduit 186. It can
therefore be seen that the apparatus shown in FIG. 41 is arranged
to allow the input of boneless meat and carbon dioxide, such as
boneless beef transferred via conduit 150 in the direction shown by
arrow 152 and fluid carbon dioxide via conduits 142 and 156 in
directions shown by arrows 136 and 154 at proportionally controlled
combined rate of mass flow and pressure. Suitable variable speed
positive displacement pumps are connected directly to all input and
output conduits connected to space 110 in such a way that a
selected pressure can be maintained within space 110. Pumps
transferring ground meat and carbon dioxide goods into space 110
via conduit 130 are controlled to provide a selected input combined
mass flow while extraction positive displacement pumps are
connected to output conduits so as to enable the extraction of
processed goods via conduits such as 132 in the direction shown by
arrow 134, conduit 160 in the direction shown by arrow 158 and
through space 106 and then in the direction shown by arrow 196. The
controlled pressure in space 110 is arranged such that the specific
density of the fluid carbon dioxide is maintained at a selected
value such as 57 lbs per cubic foot or more or less. The goods
transferred into space 110 are also maintained at a selected
temperature which can be adjusted by several means including
adjusting the pressure within space 110. Said beef transferred into
space 110 can be maintained at a pressure of about 500 psig.
Conduit 186 is of round cross section and having a space also of
round internal profile such that when the conduit 186 is rotated at
a selected speed any fluid goods transferred into space 110 will
stratify with the most dense materials closest to the internal
surface of conduit 186 and the least dense materials closest to the
center of conduit 186.
[0234] After separation, a first stream of fat can be extracted via
conduit 160 in the direction shown by arrow 158, and a second
stream of lean beef can be extracted via a conduit in the direction
shown by arrow 196. The apparatus shown in FIG. 41 comprises a
conduit 186 most preferably manufactured from stainless steel,
carbon steel or any other suitable rigid material capable of
withstanding the pressure required. The diameter of conduit 1286
may be in the order of 30 inches and is rigidly attached at each
end to conical profiled members each tapering and connecting to
conduits having a smaller diameter than conduit 186 and parallel
thereto. Cone 109 has an internal face 193 and cone 169 has an
internal face 171 and such internal faces are commonly known as
"beach" faces such that when an Archimedes screw shown as 190 is
rotated relative to beach face 193, the lean meat which by
centrifugal force has accumulated against the internal face of
conduit 186 is transferred along the conduit internal faces and
toward the conduit enclosed space 106 by the rotating action of the
screw. The dotted lines 113 and 181 define a central annular, space
110 which can be filled with pressurized carbon dioxide gas having
been transferred therein via conduit 108 at a suitable pressure
such as about 480 psig or less or more, and such that when lean
meat is transferred across the internal beach face of cone 109, the
dense fluid (liquid) carbon dioxide which occupies the annular
space defined by dotted lines 173 and 162 is not carried with the
lean meat and is displaced by gaseous carbon dioxide and in such a
way that the lean meat (beef) transferred into and through conduit
195 along space 106 does not carry excessive quantities of carbon
dioxide therewith.
[0235] The annular space defined by and between dotted line 162 and
the internal face of conduit 186 shows a fraction of the internal
space of conduit 186 where the most dense material, i.e., lean meat
such as lean beef will accumulate; the dotted lines 162 and 172
define the outer extremities of an annular space wherein fluid
and/or liquid carbon dioxide will accumulate and the annular space
defined between dotted lines 172 and 181 comprises the annular
space in which the least dense ground meat fat component will
accumulate after centrifuging therein.
[0236] The assembly shown in FIG. 41, comprising conduit 186, cone
109, conduit 195, and cone 169 with conduit 137, are rigidly
connected to provide the outer sealed and gas tight vessel 186 and
which is located and held captive by drive wheels 104, 202, 112,
178, 131, and 163 which can provide a means to drive the centrifuge
vessel 186 at any suitable selected speed and as required. The main
centrifuge conduit 186 can in this way be driven by drive wheels
112 and 178 such that conduit 186 rotates at a selected speed such
as 500 rpm or more or less and in such a way that a centrifugal
force which can be measured in units of G-force wherein 1 G is the
equivalent of the gravitational force of the earth. Drive wheels
112 and 178 may have the capacity to rotate centrifuge conduit 186
at such speed that a separating force equal to as much as 3000G can
be applied to goods transferred into space 110 and as defined by
the internal surface of conduit 186. In this instance the
centrifuge assembly as shown in FIG. 41 is arranged such that the
internal space can be pressurized up to any suitable pressure but
most preferably in this instance, in the order of approximately 480
psi or less or more. Inlet conduits and extraction ports are all
connected to positive displacement pumps or suitable valves
arranged such that a controlled quantity of goods can be
transferred into space such as 118 and extracted there from under
controlled inlet and outlet pressures corresponding to an input
mass flow and an output mass flow. The total quantity of goods
transferred therein are maintained at a controlled and adjustable
pressure of between 300 psig and 1100 psig but most preferably at
about 480 psig (and temperature of about 38.degree. F.) and at a
rate of, for example 250 gallons per minute (gpm), and therefore a
similar quantity will therefore be extracted. A grinder 148 driven
via a drive 200 connected to a variable speed motor that may be
hydraulic or servo electric of suitable horse power such as 100 hp
is arranged such that boneless beef transferred there through via
conduit 150 is ejected into space 146. Space 146 is enclosed by a
suitable profiled pressure vessel 143 to which conduits 156 and 142
are rigidly connected to enable the transfer of pressure and
temperature controlled liquid carbon dioxide in the direction shown
by arrows 136 and 154 into space 146 and in such a way that the
liquid carbon dioxide and ground meat will mix thoroughly in part
due to an aggressive turbulence created by the streams of ground
meat and liquid CO2 combining at a confluence in space 146 and in
such volume that a substantially thoroughly blended mix is
transferred along conduit 130 through space 174. A bearing 144 is
provided to allow conduit 130 to rotate freely as required while
maintaining a suitable gas tight pressure seal so as to ensure that
goods and/or fluid or liquid CO2 does not escape. Other such
bearings arranged so as to be sealed thereby preventing escape of
CO2 gas or fluid are provided at 166, 164, and 138, 198 and 102,
and at any other places where required. A series of paddles in the
form of an Archimedes screw are arranged in an assembly contained
within conduit 186 such that after the centrifugal processing of
ground meat into separate stratified concentric, annular layers,
the fat component can be extracted via conduit 160 and the lean
component extracted via conduit 199. A shaft comprising section 108
and 130 are attached to provide a fabrication wherein an Archimedes
screw comprising at least one continuous spiral member such as
shown as 194, 188, 128, and arranged such that goods stratifying at
annular space 122 forming an annular ring around the center of the
Archimedes screw are transferred from space 110 and ultimately
through conduit 160 in the direction shown by arrow 158. The
Archimedes screw assembly is arranged with a first internal screw
and a second external screw. Said first internal screw comprising a
continuous stainless steel spiral including 194 and 128 which can
be rigidly attached relative to external Archimedes screw member
shown at 190 and 120, however an annular space indicated by 125 and
192 (and located between the innermost boundary of the lean outer
section at dotted line 105 and dotted line 173 which marks the
outermost boundary of the annular space 122 in which fat can
accumulate) comprises predominantly liquid carbon dioxide other
than lean or fat particles that are in transit during the ground
beef separation process. The Archimedes screw fabrication can also
be provided with a hollow central conduit wherein a first conduit
section 174 allows the input of ground meat blended with carbon
dioxide there through and into the internal space of conduit 186
via ports 114 and 182, immediately following transfer into space in
conduit 186, ground meat is carried by the rotating motion of
conduit 186 thereby generating a centrifugal gravitational force
that results in the stratification in concentric annular spaces
such as shown at 122, where the least dense material, comprising
fat, will tend to accumulate; concentric annular space 193 in which
liquid carbon dioxide will tend to accumulate; and space at 118 in
which the most dense, lean, component of the ground meat, will
accumulate. Another centrally disposed annular space 110 can be
filled with gaseous carbon dioxide, transferred therein, at conduit
99 and through aperture such as 204 at controlled pressure and
corresponding density. In this way the Archimedes screw fabrication
is driven by a suitable means attached via shaft 108 at end at 100
such that the rotation of the two concentric Archimedes screws
shown as 188 for the inner screw for fat transfer into conduit 160
and 120 for outer screw for lean transfer into conduit 195, are
arranged to correspond with the rotating of centrifuge conduit 186.
In the first disclosed embodiment both screws are fixed rigidly
together and therefore must rotate in the same direction while also
facilitating the transfer of the fat and lean in opposite
directions. This is enabled by the direction of each screw in that
if a first concentric Archimedes screw has a left handed spiral,
then the other concentric Archimedes screw must be a right handed
screw. However, it should be noted that two independent screws,
independently driven and having the same hand and direction of
spiral must both be driven by independent driving means in opposite
rotating directions to enable transfer of fat in a first direction
and lean in the opposite direction; such a configuration can be
provided.
[0237] More particularly, a planetary gear arrangement can be
provided so as to connect the outer conduit 186 via an end section
and shaft 108, through a planetary gear arrangement having a
suitable ratio such that the Archimedes screw assembly will rotate
relative to 186 at a speed sufficient to transfer all stratified
goods from within the centrifuge at a suitable rate approximately
equal to the rate of mass flow of goods transferred into said
conduit 186. Ground meat and liquid carbon dioxide transferred into
spaces such as 118 and 110 will stratify in such a manner that the
lean component of the ground meat being of greater density than the
fat component, will stratify within space defined by the outer
annular ring defined by dotted lines 105 and 162 and against the
inner surface of conduit 186 such as into space 176 and generally
between the inner surface of 186 and a line shown by dotted lines
162 and 105. Fat component will stratify generally within dotted
lines shown on either side of space 122 and 172. Liquid CO2 will
accumulate in the space 118 defined by dotted lines 105 and 113 and
in space 172 flanked by dotted lines 173 and 181. As the Archimedes
screw assembly rotates, lean meat is carried by the Archimedes
screw comprising at least one continuous spiral strip of steel such
as shown by 190 and 120 thereby transferring the lean beef along
the internal surface of cone 109 toward a centrally disposed
conduit 106 across face 193 and into conduit space 106 and there
from through conduit 199 in the direction shown by arrow 196. A
positive displacement pump is connected directly to conduit 199 and
transfers goods there through at a controlled rate proportional to
the ground meat being transferred into the space in conduit 186.
Ports 126 and 170 in conduits 169 and 125 allow surplus liquid CO2
to be transferred through space 168 into annular manifold 165 and
through conduit 132 in the direction shown by arrow 134. Conduit
132 is connected directly to a pressure and mass flow controlling,
second positive displacement pump. A third pressure and mass flow
controlling, positive displacement pump is connected directly to
conduit 160 such that fat can be extracted there through in the
direction shown by arrow 158. It can therefore be seen that first,
second and third positive displacement pumps (not shown)
respectively connected directly to conduits 199, 132 and 160, are
controlled via a central computerized controlling system in such a
manner that goods transferred by means of controlled variable speed
positive displacement pumping in the direction shown by arrow 152
and through grinder 148, plus liquid carbon dioxide transferred
through conduits 156 and 142 which is also transferred there
through by positive displacement pumping means are substantially of
equal mass and balanced such that the mass of goods pumped into
space within conduit 186 are equal to the mass of goods pumped from
the space within conduit 186. Additionally, conduit 108 provides a
means of injecting gaseous phase carbon dioxide into space such as
110 via apertures such as 204. In this way, the quantity of liquid
CO2 that is transferred from the vessel 186 with goods can be
minimized. Gaseous phase carbon dioxide or any other suitable gas
such as nitrogen and/or a blend of carbon dioxide and carbon
monoxide, wherein the carbon monoxide content is not more than 0.4%
by volume (or weight) is transferred into space 110 at a controlled
mass flow and maintained at a suitable volume in space 110. In
summary it can be seen that fat accumulating at layer 122 and 172
can be transferred from the apparatus via conduit 160 by rotating
the Archimedes screw assembly and simultaneously lean meat
accumulating in spaces at 176 and 119 is transferred through
conduit 195 into space 106 and via conduit 199 in the direction
shown by arrow 196, and liquid carbon dioxide is extracted via
conduit 132 in the direction shown by arrow 134. The combined mass
flow of goods extracted through conduits 199, 132, and 160 is
measured by positive displacement and controlled in direct
proportion to the goods transferred through grinder 148 and space
146, blended with liquid carbon dioxide and pumped into the space
within the separating system including space 192 and or 110, for
example. Liquid carbon dioxide extracted via conduit 132 can be
recycled after sanitizing, filtering and adjusting so as to meet
specified pressure and temperature settings as required, and into
conduits 142 or 156 by positive displacement pumping from and into
the spaces within the centrifuge body 186. The temperature of
liquid CO2 is generally required to be maintained in the order of
about 38.degree. F. or less or more.
[0238] In yet another preferred embodiment a pair of (two)
separators, similar to the apparatus shown in FIG. 41, can be
arranged such that meat processed in a first separator can be
transferred under selected pressure, directly into pre-blender 3412
via a sealed, gas tight first conduit and a second stream of
processed meat can be transferred under pressure from either the
first separator or a second separator directly into pre-blender
3416. In this way, two streams of processed meat can be further
measured, combined and/or treated according to the disclosure
associated with FIG. 40 while the processing takes place under any
selected pressure (and controlled temperature). Either or both of
the streams transferred into pre-blenders 3412 and/or 3416 from a
single or two independent separators (as shown in FIG. 41) can be
transferred directly from a first separator such as from extraction
conduit shown with arrow 196 therein or for example conduit 160 in
the direction shown by arrow 154, directly to any suitable
pre-blender such as 3412 and 3416 shown in FIG. 40. Positive
displacement pumps provided so as to control mass flow of material
streams transferred via any of the conduits connected to equipment
disclosed in association with FIGS. 40 and/or 41 can be provided to
control input and output pressures as required.
[0239] Centrifuges and most particularly "decanting" style
centrifuge equipment such as equipment, manufactured by B & P
Process Equipment, which can be seen at website
http://www.bpprocess.com/ or as manufactured by Centrisys
Corporation, 9586 58th Place Kenosha, Wis. 53144, which can be seen
at website http://www.centrifuge-systems.com/ do not provide for
pressurized, temperature controlled and enclosed processing
capability for the "3 phase" separation of two solids and one
liquid. The equipment disclosed herein does provide for the
separation of two solids (i.e., fat and lean beef) and one liquid
(liquid CO2 ) and wherein the liquid (CO2 ) is a gas at ambient
atmospheric conditions. In this way the liquid CO2 can be used as
an agent facilitating the separation of the two solids (fat and
lean beef) and after use of the liquid for this purpose, the liquid
evaporates leaving no residue with the solids.
[0240] While the preferred embodiment of the invention has been
illustrated and described, it will be appreciated that various
changes can be made therein without departing from the spirit and
scope of the invention.
* * * * *
References