U.S. patent application number 10/775295 was filed with the patent office on 2004-08-19 for single strength juice deacidification incorporating juice dome.
This patent application is currently assigned to Tropicana Products, Inc.. Invention is credited to Alvarez, Marcelo Perez, Chu, Osvaldo A., Chung, Yongsoo, Lineback, D. Scott, Pepper, Mark A..
Application Number | 20040161505 10/775295 |
Document ID | / |
Family ID | 25512227 |
Filed Date | 2004-08-19 |
United States Patent
Application |
20040161505 |
Kind Code |
A1 |
Chung, Yongsoo ; et
al. |
August 19, 2004 |
Single strength juice deacidification incorporating juice dome
Abstract
A process for deacidifying single strength juice, including not
from concentrate (NFC) juice, uses an ion-exchange column. The
process includes flowing water into the resin column and draining a
fraction of the water from the column to create a head space in the
column above the resin beads. Single strength juice is then
introduced into the head space and into the resin column. Water is
drained from the column until an SOI criterium is met. Single
strength juice continues to be introduced into the resin column and
treated liquid is directed to the production of deacidified single
strength juice, typically until such time as the acidity of the
treated liquid exceeds a pre-determined value. Treated single
strength juice is removed from the resin column to create a head
space in the column. Water then is introduced into the head space
and liquid passes through the exit port.
Inventors: |
Chung, Yongsoo; (Bradenton,
FL) ; Chu, Osvaldo A.; (Sarasota, FL) ;
Lineback, D. Scott; (Bradenton, FL) ; Pepper, Mark
A.; (Bradenton, FL) ; Alvarez, Marcelo Perez;
(Bradenton, FL) |
Correspondence
Address: |
Stephen B. Heller
Cook, Alex, McFarron, Manzo, Cummings & Mehler
Suite 2850
200 West Adams
Chicago
IL
60606
US
|
Assignee: |
Tropicana Products, Inc.
Bradenton
FL
34208
|
Family ID: |
25512227 |
Appl. No.: |
10/775295 |
Filed: |
February 10, 2004 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
10775295 |
Feb 10, 2004 |
|
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|
09967041 |
Sep 28, 2001 |
|
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|
6730343 |
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Current U.S.
Class: |
426/271 |
Current CPC
Class: |
A23L 2/02 20130101; A23L
2/78 20130101; A23L 5/273 20160801; A23L 2/08 20130101; A23L 2/06
20130101 |
Class at
Publication: |
426/271 |
International
Class: |
C12H 001/04 |
Claims
1. A process for deacidifying single strength juice including not
from concentrate (NFC) juice using an ion-exchange column having a
lower volume portion filled with acid-adsorbing resin beads and
having an upper volume portion within which the resin beads are not
present, the lower volume portion having an exit port, a first
inlet port opening into the upper volume portion at an upper
location spaced a given distance above the resin beads, a second
inlet port opening into the upper volume portion at a lower
location which is spaced a distance above the resin beads which is
less than said given distance, the process comprising: introducing
water into the resin column; draining a fraction of the water from
the column through the exit port to create a head space in the
column above the resin beads; introducing untreated single strength
juice which meets SOI criteria for the single strength juice into
the resin column through the second inlet port and into the head
space; introducing untreated single strength juice which meets SOI
criteria for the single strength juice into the resin column
through the first inlet port; draining water through the exit port
to provide an outflowing treated liquid and continuing the draining
until the outflowing treated liquid meets or exceeds the SOI
criteria for the single strength juice; continuing to introduce
untreated single strength juice through the first inlet port and
directing the outflowing treated liquid to production of
deacidified single strength juice; removing treated juice from the
resin column so as to create a head space in the column;
introducing water through the second inlet port and into the head
space in the column; and introducing water through the first inlet
port passing liquid through the exit port to provide an outflowing
liquid, and continuing the passing until the outflowing liquid no
longer meets the SOI criteria for the single strength juice, at
which time treated liquid is no longer directed to production.
2. The process of claim 1 wherein the untreated single strength
juice is introduced into the resin column through the second inlet
port until the head space is filled with untreated single strength
juice.
3. The process of claim 1 wherein the untreated single strength
juice is introduced into the resin column through the first inlet
port simultaneously with the draining of the water through the exit
port.
4. The process of claim 1 wherein the single strength juice is NFC
citrus juice and the outflowing liquid is first directed to
production of deacidified NFC citrus juice when the brix of the
liquid flowing through the exit port exceeds a minimum brix value
component of the SOI criteria for the single strength NFC
juice.
5. The process of claim 1 wherein the water is introduced into the
resin column through the second inlet port until the head space in
the column is filled.
6. The process of claim 1 wherein the water is introduced through
the first inlet port simultaneously with the passing of liquid
through the exit port.
7. The process of claim 1 further comprising recovering the treated
liquid of the draining procedure for further processing into juice
products which need not meet SOI criteria for the single strength
juice.
8. The process of claim 1 further comprising recovering the treated
liquid from the passing procedure for further processing into juice
products which need not meet SOI criteria for the single strength
juice.
9. The process of claim 1 wherein the continuing procedure ceases
when the outflowing treated liquid has a pH which exceeds a
predetermined value.
10. The process of claim 9 wherein the predetermined value is
4.5.
11. The process of claim 9 wherein the pH predetermined value is
4.3.
12. A process for deacidifying single strength juice including not
from concentrate (NFC) juice using an ion-exchange column having a
lower volume portion filled with acid-adsorbing resin beads and
having an upper volume portion within which the resin beads are not
present, the lower volume portion having an exit port, the process
comprising: introducing water into the resin column; draining a
fraction of the water from the column through the exit port to
create a head space in the column above the resin beads;
introducing into the head space untreated single strength juice
which meets SOI criteria for the single strength juice; draining
water through the exit port to provide an outflowing treated liquid
and continuing the draining until the outflowing treated liquid
meets or exceeds the SOI criteria for the single strength juice;
continuing to introduce untreated single strength juice and
directing treated liquid to production of deacidified single
strength juice; removing treated single strength juice from the
resin column so as to create a head space in the column; and
introducing water into the head space in the column, passing liquid
through the exit port to provide an outflowing liquid, and
continuing the passing until the outflowing liquid no longer meets
the SOI criteria for the single strength juice, at which time
treated liquid is no longer directed to production.
13. The process of claim 12 wherein the untreated single strength
juice is introduced into the resin column until the head space is
filled with untreated single strength juice.
14. The process of claim 12 wherein the untreated single strength
juice is introduced into the resin column simultaneously with the
draining of the water through the exit port.
15. The process of claim 12 wherein the single strength juice is
NFC orange juice and the outflowing liquid is first directed to
production of deacidified NFC orange juice when the brix of the
liquid flowing through the exit port exceeds a minimum brix value
criteria of the SOI for NFC orange juice.
16. The process of claim 12 wherein the water is introduced into
the resin column until the head space in the column is filled.
17. The process of claim 12 wherein the water is introduced into
the column simultaneously with the passing of liquid through the
exit port.
18. The process of claim 12 further comprising recovering the
treated liquids of the draining procedure for further processing
into juice products which need not meet SOI criteria of single
strength juice.
19. The process of claim 12 further comprising recovering the
treated liquid from the passing procedure for further processing
into juice products which need not meet SOI criteria of single
strength juice.
20. The process of claim 12 wherein the continuing procedure ceases
when the outflowing treated liquid has an acidity which exceeds a
predetermined acidity value.
21. The process of claim 20 wherein the predetermined acidity value
is a titratable acidity of about 0.6 weight percent.
22. A process for making a low-acid single strength juice including
not from concentrate (NFC) juice product, comprising: providing an
initial single strength juice flow having suspended solids and a
known brix; diverting from the initial single strength juice flow a
first portion of the single strength juice from a second portion of
the single strength juice; separating out the suspended solids from
the first portion of the single strength juice to provide a
solids-reduced single strength juice having not greater than about
3 volume percent suspended solids based upon the total volume of
the solids-reduced single strength juice; providing an ion-exchange
column having a lower volume portion filled with ion-adsorbing
resin beads and having an upper volume portion within which the
resin beads are not present, the lower volume portion having an
exit port, a first inlet port opening into the upper volume portion
at an upper location spaced a given distance above the resin beads,
and a second inlet port opening into the upper volume portion at a
lower location which is spaced a distance above the resin beads
which is less than said given distance; introducing water into the
resin column; draining a fraction of the water from the column
through the exit port to create a head space in the column above
the resin beads; introducing the solids-reduced single strength
juice into the resin column through the second inlet port and into
the head space; introducing the solids-reduced single strength
juice into the resin column through the first inlet port; draining
water through the exit port until the brix of the outflowing
treated liquid exceeds a pre-determined minimum value relative to
the brix of the initial citrus juice flow; continuing to introduce
solids-reduced single strength juice through the first inlet port
and directing treated liquid to production of deacidified single
strength juice; removing treated single strength NFC juice from the
resin column so as to create a head space in the column;
introducing water through the second inlet port and into the head
space in the column; introducing water through the first inlet port
and passing liquid through the exit port until the brix of the
outflowing liquid drops below a pre-determined value, at which time
treated liquid is no longer directed to production; and combining
the deacidified single strength juice from the ion-exchange column
with said second portion of the single strength juice flow and with
the separated suspended solids to achieve a final blend, which is a
low-acid single strength juice.
23. The process of claim 22 further comprising adding a portion of
the initial single strength juice flow to the deacidified single
strength juice immediately after deacidification to lower the pH of
the deacidified single strength juice to a value that discourages
microbial activity.
24. The process of claim 22 further comprising cooling the initial
single strength juice flow to a temperature of not greater than
about 45.degree. F. and maintaining the single strength juice at or
below this temperature throughout the process, except during
pasteurization or enzyme deactivation, if same is practiced during
the process.
25. The process of claim 22 wherein the separating procedure
reduces the suspended solids in the solids-reduced single strength
juice to less than about one volume percent, based on the total
volume of the solids-reduced single strength juice.
26. The process of claim 22 wherein the continuing procedure is
maintained until such time as the acidity of the treated liquid
exceeds a predetermined value.
27. A process for making a low-acid single strength juice including
not from concentrate NFC juice product, comprising: providing an
initial single strength juice flow having suspended solids and a
known standard of identity (SOI); diverting from the initial single
strength juice flow a first portion of the juice from a second
portion of the juice; separating out the suspended solids from said
first portion juice to provide a solids-reduced single strength
juice having not greater than about 3 volume percent suspended
solids based upon the total volume of the solids-reduced single
strength juice; providing an ion-exchange column having a lower
volume portion filled with ion-adsorbing resin beads and having an
upper volume portion within which the resin beads are not present,
the lower volume portion having an exit port; introducing water
into the resin column; draining a fraction of the water from the
column through the exit port to create a head space in the column
above the resin beads; introducing the solids-reduced single
strength juice into the resin column into the head space; draining
water through the exit port until the SOI of the outflowing treated
liquid meets or exceeds the known SOI of the single strength juice;
continuing to introduce solids-reduced juice and directing treated
liquid to production of deacidified single strength juice; removing
treated single strength juice from the resin column so as to create
a head space in the column; introducing water into the head space
in the column and passing liquid through the exit port until the
outflowing liquid has an SOI which does not meet or exceed the
known SOI, at which time treated liquid is no longer directed to
production; and combining the deacidified single strength juice
from the ion-exchange column with-said second portion juice flow
and with the separated suspended solids to achieve a final blend,
which is a low-acid single strength juice.
28. The process of claim 27 further comprising adding a portion of
the initial single strength juice flow to the deacidified single
strength juice immediately after deacidification to lower the pH of
the deacidified single strength juice to a value that discourages
microbial activity.
29. The process of claim 27 further comprising cooling the initial
single strength juice flow to a temperature of not greater than
about 45.degree. F. and maintaining the single strength juice at or
below this temperature throughout the process, except during
pasteurization or enzyme deacidification, if same is practiced
during the process.
30. The process of claim 27 wherein the separating procedure
reduces the suspended solids in the solids-reduced single strength
juice to less than about one volume percent, based on the total
volume of the solids-reduced single strength juice.
31. A low-acid not from concentrate (NFC) juice prepared according
to the process of claim 22.
32. The low-acid NFC juice according to claim 31, said juice being
a low-acid NFC orange juice having a titratable acidity of not
greater than about 0.6 weight percent.
33. The low-acid NFC juice according to claim 31, said juice being
a low-acid citrus juice having an acidity lower than that of the
initial single strength juice flow.
34. A low-acid not from concentrate (NFC) juice prepared according
to the process of claim 27.
35. The low-acid NFC juice according to claim 34, said juice being
a low-acid NFC orange juice having a titratable acidity of not
greater than about 0.6 weight percent.
36. The low-acid NFC juice according to claim 34, said juice being
a low-acid citrus juice having an acidity lower than that of the
initial single strength juice flow.
Description
BACKGROUND OF THE INVENTION
[0001] The present invention relates to a process and system for
processing fruit juice and to a juice deacidification process and
system utilizing ion exchange resin columns that minimizes the
amount of juice lost during the "sweeten-on/sweeten-off" ion
exchange steps.
[0002] Juice products are highly popular with consumers due to both
their taste and their nutritional value. However, some fruit
juices, such as those from citrus fruits, can have a level of
acidity that makes them disagreeable to persons with sensitive
stomachs.
[0003] Numerous individuals have been known to experience negative
effects upon ingesting different foods. A true food allergy occurs
when the immune system of the individual overreacts to certain
proteins in food. It is believed that hundreds of food ingredients
can provoke an allergic reaction. Typical foods in this regard are
nuts, peanuts, milk, eggs, fish, shellfish, soybeans and wheat.
Foods such as these can lead to symptoms including nausea, hives,
skin rash, nasal congestion, wheezing, and the like. However, most
unpleasant reactions to food are caused not by allergies but by
intolerances, which tend to be less severe than true food
allergies. Typical in this regard are lactose intolerance, sulfite
intolerance and intolerance to monosodium glutamate, red wine,
chocolate and food coloring agents. Another intolerance of some
frequency is manifested by gastral distress and/or digestive
difficulties which certain individuals experience shortly after
ingesting orange juice products.
[0004] In some circles, it is generally assumed that the relatively
high acidity of orange juice products is a primary contributor to
these negative or unpleasant experiences with orange juice products
for a small percentage of the population. For example, Kligerman et
al U.S. Pat. No. 5,665,415 and No. 5,869,119, incorporated hereinto
by reference, suggest that acidic foods or beverages such as coffee
and other beverages can be combined with calcium glycerophosphate
so as to raise the pH of the food or beverage by at least 0.5 pH
units, such as to a pH of greater than 5.4, which typically is pH
higher than desirable for superior tasting orange juice. This pH
adjustment is said to reduce the tendency of the food or beverage
to cause heartburn and other esophageal and/or gastrointestinal
distress. This approach generally follows the conventional wisdom
that ingesting antacids treats heartburn by helping to neutralize
stomach acid. This approach suggests, in general, raising the pH of
the food or beverage to well above 5.
[0005] Processes for deacidifying citrus juice have been known
since the 1960s, and commercially-viable deacidification processes
using anionic ion exchange for acid reduction of citrus fruit
juices were known by 1980. However, such processing was used for
deacidifying juice made from concentrate, which has a standard of
identity (SOI) that permits a great range of flexibility in the
processing steps with respect to the dilution and blending of the
juice product.
[0006] Since that time, "not from concentrate" or NFC juices have
become very popular with consumers because of their
"fresh-squeezed" taste. These NFC juices must meet their own SOI
criteria. Among these criteria is the avoidance of a final juice
product which has water added characteristics. Other criteria
typically include brix minimums and brix-to-acid ratio
minimums.
[0007] For example the US Food and Drug Administration sets a
standard for juices such as orange juice, including brix minimums.
In this regard 21 CFR Section 146.140, incorporated by reference
hereinto, states that finished pasteurized orange juice is to
contain not less than 10.5 percent by weight of orange juice
soluble solids, exclusive of the solids of any added sweetening
ingredients. This FDA regulation further states that the ratio of
brix to grams of citric acid per 100 ml of juice is not less than
10 to 1. The juice industry recognizes these criteria for
pasteurized orange juice or single strength orange juice as
applying to-NFC orange juice. It will be understood that these SOI
criteria are used herein with respect to NFC orange juice or
pasteurized single strength orange juice. This same concept of SOI
criteria applies as well to other pasteurized single strength
juices.
[0008] While it is anticipated that there would be a significant
market for a low acid NFC orange juice, deacidification processes
utilizing ion-exchange resin columns can easily result in the
processed juice being diluted. This is particularly true if the
ion-exchange column is designed to operate with a water/juice
interface or a "water dome" in the head space of the column above
the resin bed. Such water dilution of the processed juice is
unacceptable for NFC juices because the standard of identity
("SOI") of the juice is compromised.
[0009] Accordingly, it is an object of the present invention to
provide a process and system for deacidifying NFC juices that do
not compromise the standard of identity required for such juice
products.
[0010] More particularly, it is an object of the present invention
to provide a process and system for deacidifying NFC juices that do
not dilute the NFC juice so that NFC SOI can be maintained.
[0011] It is a still further object to deacidify NFC juices while
minimizing the amount of juice that is wasted or becomes otherwise
unuseable due to the deacidification process.
[0012] A further object of the invention is to provide an improved
single strength juice which meets SOI criteria throughout all
phases of single strength juice product collection.
SUMMARY OF THE INVENTION
[0013] These objects, as well as others that will become apparent
upon reference to the following detailed description and
accompanying drawings, are accomplished by a process for
deacidifying single strength juice, preferably not from concentrate
(NFC) juice that uses an ion-exchange column having a lower volume
portion that is filled with acid-absorbing resin beads and an upper
volume portion within which the resin beads are not present. The
lower volume portion has an exit port, while at least one inlet
port opens into the upper volume portion.
[0014] The process includes filling the resin column with water and
then draining a fraction of the water from the column through the
exit port to create a head space in the column above the resin
beads. Untreated juice is then introduced into the resin column. In
a preferred arrangement, such initial flow is through an inlet port
so as to minimize resin bed disturbance. With this arrangement,
after the head space has an adequate volume of juice, untreated
juice can be introduced into the resin column. In the illustrated
embodiment, this is through an inlet port which is at an upper
location of the upper volume portion. Water is drained through the
exit port until the outflowing treated liquid meets SOI criteria
for the single strength juice. Untreated juice continues to be
introduced, and treated juice is collected as deacidified single
strength juice until a pre-determined value is attained, such as
when a target processing volume is obtained or until the resin is
exhausted.
[0015] Treated juice is removed from the resin column to then
create a head space in the column. In one approach, this leaves the
resin beads wetted or even submerged. Alternatively, all free juice
may be displaced out of the resin bed before the next phase
introduces water into the resin bed. Water is then introduced into
the head space in the column, and liquid passes through the exit
port until the outflowing liquid does not meet SOI criteria for the
single strength juice, at which time this liquid is no longer
directed to production.
BRIEF DESCRIPTION OF THE DRAWINGS
[0016] FIG. 1 is a schematic diagram illustrating a process for
producing single strength low acid juice products incorporating
ion-exchange resin columns in accordance with the present
invention.
[0017] FIG. 2 is an enlarged schematic view of a pair of
ion-exchange resin columns for performing the process of the
present invention.
[0018] FIG. 3 illustrates the deacidification process of the
present invention with a single ion-exchange resin column (it being
understood that the other resin column of the pair that is not
shown is being regenerated simultaneously with the deacidification
being carried out in the first resin column).
[0019] FIGS. 4A-4C are plots of pH of blended juice versus ratio of
untreated juice to treated juice in the blended juice for various
Bed Volumes of juice subjected to the deacidification process of
the present invention, the untreated juice of this illustration
having a pH of 3.94 and a titratable acidity of 0.61% for FIG. 4A,
a 3.82 pH and 0.65% titratable acidity for FIG. 4B, and a 3.65 pH
and 0.75% titratable acidity for FIG. 4C.
DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS
[0020] The method of the present invention is directed to the
deacidification of single strength fruit or vegetable juice,
especially NFC citrus juice, and is part of the process of
producing a low-acid single strength juice product from standard
single strength juice.
[0021] Deacidification of citrus juice may take place in any number
of known devices. For example, the form of ion exchange resin
equipment used in deacidification of citrus juice may be a
flow-through column and/or a continuous system or semi-continuous
system. Another possibility is the use of resins in a bed
formation, such as in an overall batch approach. Ion exchange
technology may be utilized to deacidify juice in any number of
possible devices, provided that the resins are allowed to contact
the juice during the process.
[0022] The resins used in ion exchange technology may likewise be
of a wide variety. Resins of any level of binding affinity may be
used, depending on the acidity of the juice. In one preferred
embodiment, the resin used is a weakly-basic, anionic exchange
resin, often a polystyrene copolymer which contains a tertiary
amine group as a functional group. This weakly-basic resin is
preferred because of its ability to pull organic acids such as
citric acid from the juice, thereby producing a deacidified juice
stream.
[0023] Examples of other commercial resin systems include those
incorporating ion exchange resins such as anionic polystyrene
copolymers which release chloride groups and basic anionic
polystyrene resins having quaternary ammonium active groups.
Specifically, resins such as Amberlite IRA-67, Amberlite IRA-95,
Dowex 67, Dowex 77 and Diaion WA 30 may be used.
[0024] Deacidification of juice takes place as a juice stream is
passed through or otherwise contacts the resin bed. The juice used
may be any fruit or vegetable single strength juice which has not
been concentrated, preferably an NFC citrus juice, including orange
and grapefruit, the most preferred juice being orange juice. To
deacidify the citrus juice using ion exchange technology, a juice
stream comes in contact with the ion exchange resins. The preferred
method uses a juice stream that is passed through the resin
structure, such as the resin bed or column. As the juice contacts
the resins, ion exchange takes place in accordance with known
principles.
[0025] In ion exchange deacidification, when the juice stream comes
in contact with the resin, the ions of the juice are exchanged with
those of the resin. In the preferred embodiment, acidic juice comes
in contact with, and is attracted to, the weakly-basic polystyrene
resin. When citrus juice is treated, the ion exchange resin adsorbs
the citrus ions of the citrus juice. Adsorption is the accumulation
of ions on a resin pore surface, resulting in a relatively high
concentration of the ions at the resin's surface. After citrate
ions of the juice stream are adsorbed by the resin, the stream is
substantially less acidic.
[0026] The general process for producing a low-acid single strength
juice product such as low-acid NFC orange juice typically includes
the following steps: (a) heat treatment, if needed, to inactivate
the pectin esterase enzyme present in the single strength juice;
(b) centrifugation for solid/liquid separation to produce a
solids-reduced juice (i.e., juice with generally less than 3 volume
percent, typically less than 2 volume percent, and, preferably, not
more than 1 volume percent, of suspended solids); (c)
deacidification of the solids-reduced juice, with untreated juice
optionally being added to the deacidified juice immediately after
the deacidifying process to adjust the pH to a level (i.e., below
about 4.5) that is unfavorable to microbial activity; (d) blending
the deacidified solids-reduced juice with the solids that were
separated in step (b) and additional untreated juice to the extent
necessary to obtain the desired final acidity level; (e) adding
additional ingredients such as oils, minerals and vitamins, as
desired; (f) mixing for a final time; and (g) packaging.
Pasteurization and the performance of quality control checks
typically will be carried out at suitable stages of the process.
With respect to step (b), other solid/liquid separation techniques,
such as membrane filtration, decanting or the use of rotary filters
or finishers, and the like may be used in place of
centrifugation.
[0027] The general overall process may be run at various
temperatures. However, it is preferred that the overall process be
performed at refrigerated temperatures (i.e., less than about
45.degree. F. and preferably between about 35.degree. F. and
45.degree. F.) to produce a higher quality juice product. It has
been determined that the quality of the resulting juice product is
greatly enhanced by conducting the process at these low temperature
levels, even though this would be expected to reduce the efficiency
of the solid/liquid separation of step (b) and the ion exchange
efficiency of the resin of step (c). It has been found that very
satisfactory results and minimal negative operational aspects have
been experienced.
[0028] A schematic diagram illustrating steps (b) through (f) of
the process of producing a low-acid single strength juice product
is shown in FIG. 1, as well as the system by which it is carried
out. In this illustration, single strength orange juice (usually
pasteurized) enters the system at 10 and flows into a centrifuge
feed tank 12. Simultaneously, a portion of the single strength
juice also is directed into a blend tank 14 for later combination
with the deacidified juice. Optionally, a portion of the untreated
juice may be diverted to a bypass line 15 so that it can be added
back to the treated juice immediately after deacidification, the
importance of which is discussed below.
[0029] From-the centrifuge feed tank 12 the juice flows into one or
more centrifuges 16 for separation of the solids from the juice.
The separated solids (and a small quantity of juice) are diverted
directly to the blend tank 14, or as illustrated into a recombine
tank 17, while the remainder is tested to determine whether
sufficient separation has been accomplished.
[0030] This testing provides a volume percent value, based upon the
total volume of the juice, measured by the method described by D.
Kimball in "Citrus Processing Quality Control and Technology,"
1991, incorporated by reference hereinto. This measurement
procedure is summarized generally as follows for orange juice.
11.8.degree. brix juice at 26.degree. C. is poured into a 50 ml
centrifuge tube, which is inserted into a centrifuge. For a
centrifuge with a spacing of 11.5 inches, the centrifuge is run at
1500 rpm for 10 minutes. The pulp level is read, and the value is
divided by 50 ml to determine the volume percent.
[0031] In the illustrated embodiment, the thus determinied
suspended solids in the centrifuged juice is selected to be not
greater than 1 volume percent. Acceptable results can also be
obtained for suspended solids of up to about 3 volume percent if
the average particle size distribution is 10 microns or less.
Usually, the suspended solids will be less than about 2 volume
percent of the total volume of the centrifuged juice. The quantity
of suspended solids is limited by the ability of the reduced-solids
juice to easily pass through the resin column. If the desired
suspended solids volume is not attained, the solids-reduced juice
is returned to the feed tank 12 for further centrifugation or other
separation, or same can be transferred to the blend tank 14 as
desired.
[0032] If the suspended solids are at or below the selected maximum
volume percent, the juice then is treated or otherwise processed to
inactivate or remove enzyme, for example by heat treatment. This
also can be used to pasteurize, if needed. If the juice has been
previously thus treated or pasteurized, it goes directly from the
centrifuge 16 to the ion exchange resin columns 18, 20 for
deacidification in accordance with the present invention. If not,
the juice is directed from the centrifuge 16 to a balance tank 22.
It is then rapidly heated at 24, and then chilled, before being
directed to the resin columns 18, 20.
[0033] As illustrated, the process and system utilize a pair of
identical ion-exchange resin columns 18, 20. This permits
continuous operation of the system, as one column of the pair can
be recharged (typically with a basic medium such as but not limited
to sodium hydroxide--NaOH, or potassium hydroxide--KOH, or a
combination of bases such as these), while the other resin column
in the pair is being used to deacidify the juice.
[0034] With reference to FIG. 2, each resin column 18, 20 is
partially filled (approximately half-filling being shown) with ion
exchange resin beads 26. The composition of such beads is
well-known. See, for example, U.S. Pat. Nos. 4,522,836 and
4,666,721 which are incorporated hereinto by reference. Through a
series of piping and flow control valves well known in the art, the
resin columns 18, 20 are configured to selectively admit either
juice or water.
[0035] In this illustrated embodiment, such inflow can be through
one of two inlet ports. Inlet port 28 is configured so that the
fluid flowing therethrough enters at the top of the resin column,
approximately half the column height above the top of the bed of
resin beads 26. Inlet port 30 is a "downcomer", i.e., it is
configured so that fluid flowing through it enters the resin column
only a short distance above the bed of resin beads 26.
[0036] The illustrated downcomer has a member between its outlet(s)
and the resin bed surface so that the outflow cascades and enters
the resin bed in a diffused manner so as to minimize the
disturbance of the resin beads by fluid flowing out of inlet 30. To
this end, the opening in the inlet 30 is illustrated to be spaced
above a deflector plate 31. The spacing should be adequate to allow
for a 25 percent to 30 percent expansion of the resin beads during
the course of the process. After such expansion, the bed surface
remains spaced from the port 30 or plate 31, preferably by from
about 2 to 4 inches.
[0037] The top of each resin column includes an air vent 32, as is
customary. Also customary is an exit port 34 (and valve) at the
bottom of each column, thus permitting fluid contained in the
column to be drained by gravity, or by pressure application, in a
known manner. Typically when pressure is applied, it is by air or
other gas.
[0038] In keeping with the invention, a deacidification process and
system are provided that utilize a "juice dome" in the resin column
to insure adherence to SOI requirements for the NFC juice and to
minimize yield loss during processing.
[0039] With reference to FIG. 3, the "juice dome" deacidification
process is illustrated. Only a single resin column is illustrated,
it being understood that the other resin column of the pair is
being recharged and is, thus, off-line. Any number of resin columns
can be provided to satisfy flow requirements. In its INITIAL
condition, the illustrated resin column is freshly recharged and
filled with water, so that the portion of the resin column above
the level of the resin beads (i.e., the "dome" of the column) is
substantially filled with water. This illustrates the "charged"
phase.
[0040] The dome then is transitioned from being filled with water
to being filled with juice. Thus, as shown in STEP 1A, water is
drained from the column to create a head space in the dome. This
may be accomplished by either the force of gravity or by the
application of air pressure to the top of the column. During this
phase of transition from the charged phase to a "sweeten-on" phase,
preferably only a portion of the water is drained from the column,
so that the resin beads remain wetted, whether completely submerged
or not. Keeping the resin beads wetted helps to insure that the
beads do not dry out, which can result in the empty spaces in the
beads filling with air. Such captured air cannot be easily
displaced, thus reducing the surface area of the beads available
for deacidification, and reducing the efficiency of the
process.
[0041] Then, as shown in STEP 1B, the single strength juice flows
into the dome, or head space. The flow continues until a desired
volume of juice is positioned within the dome, for example until
the upper volume portion is filled. Preferably, this flow
introduces the single strength juice from the middle-level or
downcomer inlet port 30, while air is vented through the top of the
column. In this step, when the dome is to be filled completely with
juice, the flow of juice to the column is stopped once the upper
volume portion is full. This is the "juice dome" formation
stage.
[0042] The next steps constitute a transition to the production
stage of the deacidification process. This is known as the
"sweeten-on" phase of the deacidification process and system, and
is shown as STEP 2A, STEP 2B, and STEP 2C. First, as shown in STEP
2A, water is pushed out of the resin bed by introducing single
strength juice into the column, preferably through the top inlet
port 28. The water is drained from the column.
[0043] At a selected point, the outflow need no longer be drained
as waste, but it can be collected for recovery of juice components
as the juice content increases. As can be appreciated, the
"interface" is a mixture of water and juice or diluted juice. When
this outflows, it can be collected for uses other than as single
strength or NFC juice. This outflow can be monitored by tracking
parameters such as brix and/or color. Generally, at least one SOI
criteria parameter, and if possible multiple parameters, will be
tracked. Also, this can be determined by tracking time of flow at a
known flow-rate. As shown in illustrative STEP 2B, the diluted
juice stream is diverted to a secondary stream recovery tank and
can later be used in other products which are not restricted by the
SOI requirements for the single strength juice.
[0044] Then, when it is determined that the deacidified juice
exiting the column meets SOI criteria of the single strength juice,
product can be collected as deacidified single strength or NFC
juice. This is generally shown in STEP 2C. With the invention, this
is accomplished after a turn over of as little as one resin Bed
Volume. This is the volume of the beads within the vessel. Somewhat
greater than one Bed Volume can be displaced before diverting the
outflow to production, such as after about 11/2 Bed Volumes, to
provide a measure of safely to assure that only juice meeting SOI
criteria is collected as single strength or NFC product.
[0045] Juice continues to be introduced into the column such as
through the top inlet port 28, and the deacidified juice continues
to be directed to production, as shown in STEP 3. This production
phase continues until production is stopped according to program.
This may be at a point when the acidity of the deacidified juice
has increased to a certain pre-determined value, meaning that the
resin beads are "spent" and that the resin column needs to be
regenerated.
[0046] A further transition phase transforms the resin column from
the spent state to the "sweeten-off" phase. The dome of the column
is transitioned from containing juice to containing water, as shown
in STEP 4A and STEP 4B. First, as shown in STEP 4A, the juice in
the dome is pushed out of the column by either gravity or air
pressure at the top of the resin bed, usually with the deacidified
juice exiting the column continuing to be directed to production.
Then, as illustrated in STEP 4B, the outlet of the column is closed
and the dome of the column is filled by introducing water,
preferably from the middle-level or downcomer inlet port 30 (unless
resin disturbance is not a concern), with air being vented through
the top of the column. Water is introduced into the column until
the dome is completely filled, at which time water flow to the
column is stopped.
[0047] Next comes the "sweeten-off" phase of the process and
system, as illustrated in STEP 5A, STEP 5B, and STEP 5C. First, as
shown in STEP 5A, the outlet is opened and more water is introduced
into the column through the top outlet port 28 so that the
remainder of the deacidified juice is pushed out of the resin bed,
usually going to production. This continues until the juice exiting
the column no longer meets SOI criteria for the juice. In most
cases, at least 1/4 bed volume of juice will be recovered as
product at this stage. This has been found to provide a good
measure of safety to insure SOI is maintained.
[0048] Then, as shown in STEP 5B, the interface or mixture of water
and juice or diluted juice is pushed out of the column by
additional water entering through inlet port 28, and the diluted
juice stream preferably is diverted to the secondary stream
recovery tank described above. The timing of this diversion away
from production is determined as generally discussed herein with
respect to the "sweeten-on" phase. Typically this-will be at a
maximum of one bed volume of outflow.
[0049] Then, when the outflow of the diluted juice stream becomes
so dilute that it is no longer economically feasible to collect,
the diluted juice stream is diverted, such as to the drain, as
shown in STEP 5C. The column is then taken off-line for recharging
in accordance with generally known principles, at the end of which
it is returned to the charged phase, typically being filled with
water as in the INITIAL step of FIG. 3.
[0050] By use of this "juice dome" process and system, the juice
yield has been increased approximately 10 percent, as compared to a
standard method using a "water dome." Specifically, the "juice
dome" facilitates control of the water-juice interface in the resin
column. As a consequence, the number of Bed Volumes of liquid that
are processed by the resin columns during the transitions to and
from the production phase of the deacidification process is
minimized, thus minimizing the dilution of the NFC or single
strength juice that would otherwise be waste or be suitable only
for non-NFC juice products and the like. As little as one Bed
Volume of liquid is needed for the sweeten-on phase before single
strength SOI criteria are reached. Less than 2 Bed Volumes of
liquid are processed during sweeten-off phase before the diluted
deacidified juice is no longer suitable to recover for use in
non-NFC products and the like.
[0051] Further advantages accrue to the use of the deacidification
process and system described above. Specifically, the introduction
of the juice (or water) from the middle-level or downcomer inlet
port 30 to fill the dome minimizes the potential for undesirable
disturbance of the resin beads. Including the plate 31 further
enhances this advantage. Introducing the juice from the top inlet
port 28 during the juice processing portion of the procedure,
rather than through the downcomer inlet port 30, also minimizes
stagnant juice in the dome and keeps the juice that remains flowing
during processing.
[0052] After the juice is deacidified as described above, it is
directed to a batch tank or blend tank 14 for final mixing.
Preferably, this flow is first into the recombine tank 17 where it
is combined with the solids-rich flow out of the separator 16. This
combined flow then enters the blend tank 14.
[0053] At least in the initial stages of deacidification when the
resin column is most effective, i.e., the initial "Bed Volumes" of
juice passing through the column, the acidity level of the
deacidified juice may be sufficiently low--and the pH sufficiently
high--that undesirable microbial activity in the deacidified juice
could occur. Thus, as mentioned above and if desired, a portion of
non-deacidified juice may be added back to the deacidified juice
immediately upon its flow out of the resin columns in order to
raise the acidity--and lower the pH--of the resulting blend to a
level that discourages microbial activity. A pH of about 4.5 or
below is effective for this purpose.
[0054] In practice, the immediate addition of untreated juice in a
ratio of between about 2:1 and about 1:1 with respect to the
deacidified juice may be necessary for the first 10 to 12 Bed
Volumes of deacidified juice to keep the pH lower than about 4.5.
See the plots of pH versus ratio of untreated juice to treated
juice taken at various Bed Volumes (i.e., 1, 3, 6, 9, 12, 15 and
18) shown in FIGS. 4A, 4B and 4C, which empirically show that
ratios of untreated juice to treated juice of between about 1:1 and
about 2:1 should ensure a pH of 4.5 or below. Depending upon the
precision of the pH measurement techniques or pH monitor, in
practice it can be desirable to provide a safety cushion by
targeting a lower pH, e.g., 4.4 or 4.3. After the pH of the
deacidified juice exiting the resin column drops below 4.3-4.5, the
immediate addition of untreated juice to raise the acidity is no
longer necessary.
EXAMPLE 1
[0055] The following example illustrates the process for making low
acid orange juice from NFC orange juice. The following are the
parameters for the example: the titratable acidity of the NFC
orange juice entering into the system at 10 is 0.68 percent, while
the flow rate for the NFC feed is 133 gallons per minute (gpm). The
cycle time for the process is 6 hours, resulting in a batch size of
approximately 48,000 gallons. The volume of the resin in the column
is 50 cubic feet, and the time required to regenerate the column is
3.5 hours.
[0056] From the inlet 10 to the system, 83 gpm of untreated juice
is directly diverted to the blend tank 14. The remaining 50 gpm of
untreated juice is directed to the centrifuge 12. The untreated NFC
juice has the following characteristics: Temperature (35.degree.
F.); Acidity (0.68% w/w); pH (3.8); Suspended solids (11%); Oil
(0.030% v/v); Ascorbic acid (40.9 mg/100 ml); and Calcium (81
ppm).
[0057] Of the 50 gpm of juice entering the centrifuge, 5 gpm is
directed to the blend tank 14. Centrifuging in this example is
complete if the percentage of suspended solids in the centrifuged
NFC juice is less than 1 percent. After completing centrifugation,
the juice has the following characteristics: Temperature
(35.degree. F.); Acidity (0.67% w/w); pH (3.8); Suspended solids
(1%); Oil (0.022% v/v); Ascorbic acid (39.2 mg/100 ml); and Calcium
(77 ppm).
[0058] After centrifuging, 45 gpm of juice goes directly to the
resin columns 18, 20 for deacidification. However, if the
centrifuged juice has not already been pasteurized, it is directed
to the balance tank, from which it receives heat treatment. The
juice is rapidly heated to a pasteurization temperature for a very
short duration and then immediately chilled so that the product has
a final temperature of 40.0.degree. F. The pasteurized juice then
is directed to the resin columns 18, 20 for deacidification.
[0059] After deacidification, in accordance with the steps
described above, the deacidified juice stream exiting the resin
columns has the following characteristics: Temperature (40.degree.
F.); Acidity (0-0.5% w/w); pH (9 to 4.4); Suspended solids (1%);
Oil (0.018% v/v); Ascorbic acid (31.1 mg/100 ml); and Calcium (75
ppm). Note that the acidity of the juice exiting the resin column
will vary so as to increase during the course of a cycle as the
ion-exchange resin loses its effectiveness.
[0060] The deacidified juice is then directed to the blend tank,
where it is mixed with the untreated juice to achieve the final
blend having the following characteristics: Temperature (36.degree.
F.); Acidity (0.58% w/w); pH (4.1 to 4.3); Suspended solids (10%);
Oil (0.028% v/v); Ascorbic acid (38 mg/100 ml); and Calcium (56
ppm). At this time, additional oils, minerals and vitamins may be
added. In the present example, additional calcium is added.
[0061] The blended low acid juice then is directed at a rate of 100
gpm to a pasteurizer, or, if the untreated juice has been
pasteurized, directly to a packaging line.
EXAMPLE 2
[0062] In a second example, microfiltration is used to separate the
juice and solids, rather than centrifugation. Otherwise, the basic
parameters are identical to those of Example 1. The titratable
acidity of the NFC orange juice entering into the system is 0.74
percent; the flow rate for the NFC feed is 133 gallons per minute
(gpm); the cycle time for the process is 6 hours; the batch size is
48,000 gallons; the resin bed has a volume of 50 cubic feet; and
the time required the regenerate the column is 3.5 hours.
[0063] From the inlet to the system, 83 gpm of untreated juice is
directly diverted to the blend tank. The remaining 50 gpm of
untreated juice is subjected to microfiltration. The untreated
juice has these characteristics: Temperature (35.degree. F.);
Acidity (0.74% w/w); pH (3.76); and Ascorbic acid (45.1 mg/100
ml).
[0064] Of the 50 gpm of juice being subjected to microfiltration,
10 gpm does not pass through the filter membrane and constitutes
the "retentate". The retentate is directed to the blend tank. It
has these characteristics: Temperature (65.degree. F.); Acidity
(0.80% w/w); pH (3.80); and Ascorbic acid (39.2 mg/100 ml).
[0065] The remaining 40 gpm that has passed through the filter
membrane, i.e., the "permeate", has these characteristics:
Temperature (40.degree. F.); Acidity (0.71% w/w); pH (3.74); and
Ascorbic acid (43.4 mg/100 ml).
[0066] The filtered juice goes to the resin columns at a rate of 40
gpm for deacidification in accordance with the process described
above. The deacidified juice has these characteristics: Temperature
(45.degree. F.); Acidity (0.38% w/w); pH (4.22); and Ascorbic acid
(38.0 mg/100 ml).
[0067] The deacidified juice is then directed to the blend tank,
where it is mixed with the untreated juice and retentate to achieve
the final blend having these characteristics: Temperature
(35.degree. F.); Acidity (0.61% w/w).; pH (3.86); and Ascorbic acid
(42.5 mg 100 ml).
[0068] Deacidified juices produced by the methods illustrated in
Examples 1 and 2 were similar in flavor, and both methods yielded
juices that were lower in sourness than regular orange juice which
has not been deacidified.
[0069] Thus, a method for deacidifying single strength or NFC juice
has been provided that meets objects of the present invention.
While the invention has been described in terms of a preferred
process with a specific example, there is no intent to limit the
invention to the same. Instead, it is intended to be defined by the
scope of the following claims.
* * * * *