U.S. patent application number 14/333228 was filed with the patent office on 2014-11-06 for method for dissociation of cells.
The applicant listed for this patent is Grain Processing Corporation. Invention is credited to Sarjit Johal.
Application Number | 20140328996 14/333228 |
Document ID | / |
Family ID | 34193343 |
Filed Date | 2014-11-06 |
United States Patent
Application |
20140328996 |
Kind Code |
A1 |
Johal; Sarjit |
November 6, 2014 |
Method for Dissociation of Cells
Abstract
Disclosed is a method for the dissociation of cells. Cells are
processed under conditions of pH, temperature, and shear to thereby
yield a mixture of cell wall ghosts and cytoplasm. Preferably, the
cells are jet cooked at an alkaline pH to form an intermediate
mixture, and the intermediate mixture is subsequently jet cooked.
Generally, the cells become dissociated, whereby at least one
separate cell wall component is substantially separate from the
dissociated cell walls.
Inventors: |
Johal; Sarjit; (Iowa City,
IA) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Grain Processing Corporation |
Muscatine |
IA |
US |
|
|
Family ID: |
34193343 |
Appl. No.: |
14/333228 |
Filed: |
July 16, 2014 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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12170033 |
Jul 9, 2008 |
8828708 |
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14333228 |
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10919191 |
Aug 16, 2004 |
7425439 |
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12170033 |
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60495750 |
Aug 15, 2003 |
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Current U.S.
Class: |
426/656 ;
426/523 |
Current CPC
Class: |
A23K 50/10 20160501;
C12N 1/005 20130101; A23K 10/16 20160501; C12N 1/063 20130101; A23K
40/00 20160501; A23K 50/30 20160501; A23K 10/12 20160501; A23L
33/14 20160801; C12N 1/066 20130101 |
Class at
Publication: |
426/656 ;
426/523 |
International
Class: |
A23K 1/00 20060101
A23K001/00 |
Claims
1-20. (canceled)
21. A mixture of cell wall ghost and cytoplasm prepared by steps
comprising: providing a plurality of cells; and subjecting said
cells to heat, pH, and shear under conditions sufficient to rupture
the walls of at least some of said plurality of cells to allow
cytoplasm to be released therefrom to thereby form a mixture of
ghosts and cytoplasm, said cells being cooked in a jet cooking
apparatus.
22. A mixture according to claim 21, said pH ranging from 8.5 to
10.5.
23. A mixture according to claim 21, said cells being subjected to
a temperature ranging from 140 to 160.degree. C.
24. A mixture according to claim 21, said steps including:
jet-cooking said mixture of cells in a jet-cooking apparatus to
form an intermediate mixture; and jet-cooking said intermediate
mixture to form said mixture of cell walls and cytoplasm.
25. A mixture according to claim 21, said cells comprising yeast
cells.
26. A mixture according to claim 25, said cells comprising S.
cereviasiae cells.
27. A cytoplasm mixture formed by at least substantially separating
cell wall ghosts from the mixture of claim 21.
28. A cell wall ghost mixture formed by at least substantially
separating cytoplasm from the mixture of claim 21.
29. A product formed by spray-drying the mixture of claim 21.
30. An animal feed compromising: A mixture of cell wall ghosts and
cytoplasm, said mixture having been prepared by providing a
plurality of cells; and subjecting said cells to heat, pH, and
shear under conditions sufficient to rupture the walls of at least
some of said plurality of cells to allow cytoplasm to be released
therefrom thereby forming said mixture of ghosts and cytoplasm,
said cells being cooked in a jet cooking apparatus, and at least
one other animal nutritive source.
31. An animal feed according to claim 30, said pH ranging from 8.5
to 10.5.
32. An animal feed according to claim 30, said cells being
subjected to a temperature ranging from 140 to 160.degree. C.
33. An animal feed according to claim 30, said steps including:
jet-cooking said mixture of cells in a jet-cooking apparatus to
form an intermediate mixture; and jet-cooking said intermediate
mixture to form said mixture of cell walls and cytoplasm.
34. An animal feed according to claim 30, said cells comprising
yeast cells.
35. An animal feed according to claim 34, said cells comprising S.
cereviasiae cells.
Description
RELATED APPLICATION
[0001] This application claims the benefit of prior provisional
application Ser. No. 60/495,750, filed Aug. 15, 2003, the teachings
of which application are hereby incorporated by reference.
FIELD OF THE INVENTION
[0002] The invention pertains to the dissociation of cells to
obtain nutrients and other commercially useful products
therefrom.
BACKGROUND OF THE INVENTION
[0003] Yeast and yeast metabolites are widely used in an array of
food and feed products. Baker's and brewer's yeast, for example,
are excellent sources of nutrients and flavoring agents. Nutrients
that are obtainable from cells include insoluble and soluble cell
wall polysaccharides, oligosaccharides, glucans, proteins,
peptides, nucleotides, and the like. Cells, in particular cell
walls, are also thought to absorb pathogens and consequently to
provide a measure of prophylaxis against infection.
[0004] Live cells, whole lysed cells, and cell fractions are of
particular value in feed and pet food formulations. Lysed cells and
cell fractions are thought to contain many nutritive components in
a form that is bio-available to the consuming animal. Live yeast
cells are thought to aid in digestion in ways not fully understood
at present. Whole dead cells, on the other hand, are not thought to
be of particular nutritive benefit, except possibly in ruminant
animals. The digestive tract of monogastric animals is essentially
unable to rupture the cell wall, and thus the majority of the dead
cells pass through the digestive tract and are typically excreted
whole, without releasing nutrients to the animal.
[0005] Consequently, if it is desired to obtain nutrients from dead
yeast cells, generally it is necessary to rupture the walls of the
cells to allow release of the nutrients. A number of methods are
known for rupturing yeast cells, these including mechanical,
hydrolytic and autolytic methods. Mechanical methods typically are
employed in small-scale laboratory applications. Conventional
mechanical disruption includes presses, such as the French press;
homogenizers; sonic disruptors, and so forth. In a laboratory
French press, for example, pressures as high 20,000 psi and high
shear conditions are produced by passing the cells through a small
orifice. Other devices subject the cell to different stresses but
provide the same result, that is, rupture of the cell wall. For
instance, another known apparatus, the bead beater, contains
ceramic or glass pellets that are used to crush, shear and fracture
cells. Hydrolytic procedures employ enzymes, acid, or alkali to
rupture the cell walls. Cell autolysis is a well-known process
wherein the yeast cell is subjected to digestion by its own
enzymes.
[0006] Heretofore, it is believed that it has been difficult to
extract nutrients from cells on a commercial scale, particularly
from dead yeast cells, in light of certain drawbacks with the
foregoing conventional methods. Mechanical rupture is attractive
because the cell constituents are not contaminated with extraneous
chemicals and additives. However, the costs associated with
scaling-up and implementing such systems are considerable, as has
been heretofore recognized. For instance, U.S. Pat. No. 5,756,135
issued to Seeley discusses some of the technological and economical
challenges associated with commercial-scale production of a water
insoluble yeast. Hydrolytic methods are more amenable to scale-up,
but most such methods also have shortcomings such as high cost,
long process time, or degradation/denaturation of specific
nutrients.
[0007] Accordingly, most yeast cell hydrolyzates are produced
commercially by autolysis. Yeast autolysis entails a slow reaction,
however. An autolysis reaction requires an operating temperature
that ranges from about 40.degree. C. to 60.degree. C., typically
temperatures of 50.degree. C.-55.degree. C. At these or higher
suitable temperatures, the reaction still requires a substantial
period of time ranging from several hours to days to obtain a
suitable degree of digestion. In an effort to accelerate the
autolysis reaction, the prior art has taught to employ plasmolyzing
agents, examples of which include organic solvents, salts and
hydrolytic enzymes such as protease and lipases. Nonetheless, the
autolysis reaction remains lengthy and commercially unwieldy.
[0008] A further drawback with autolysis is that the autolysis
process is amenable only for use with living cells. Dead cells
cannot be autolyzed. In recognition of this requirement, dedicated
yeast manufacturers who desire to autolyze the yeast cells are
required to take steps to preserve cell viability. In other
industries where substantial quantities of live yeast are produced
as a by-product, such as the brewing industry, live cells can be
harvested economically and can be subjected to autolysis. However,
certain industrial processes generate a substantial quantity of
dead yeast by-product that cannot be subjected to autolysis. This
is a particular problem in the production of distilled ethanol
products, wherein the distillation process kills the yeast cells,
thereby rendering the cells impossible to autolyze.
[0009] Accordingly, given the heretofore described drawbacks with
mechanical and hydrolytic methods, it is very difficult to produce
a cost-effective, high-volume yeast-derived feed or industrial
product from such dead cells. In practice, the dead yeast cells
themselves are sold as whole cells, typically into the ruminant
animal feed markets.
[0010] It would be desirable to provide a method for disassociating
yeast and other cells in a manner that allows for rupture of the
walls of the cells to release the cell cytoplasm therefrom. It
would be of particular benefit for such method to be applicable to
dead cells in addition to live cells. Such method would find a
particular applicability in the distilled ethanol industry, but
would also be useful in connection with numerous other
industries.
THE INVENTION
[0011] It has now been found that yeasts, fungi, bacteria, and
other cells (including eukaryotic cells) may be processed to
recover soluble or insoluble cell components such as proteins,
saccharides, peptides, lipids, glucans, and the like. Generally,
the cells are processed by a shearing force in the presence of an
alkaline pH and heat (i.e. temperatures above 25.degree. C.).
[0012] In accordance with the invention, a method for dissociating
cells is provided. In one embodiment of the invention, conditions
of pH, shear, and temperature suitable for dissociation of the cell
are selected, the conditions being suitable for dissociation
whereby at least one soluble dissociated molecular cell wall
component is substantially separable from the dissociated cells.
The method is intended to at least substantially completely
dissociate the cell walls, but the cells are not dissociated to
such an extent that the molecular constituents of the cell walls
are reduced to simple molecules. The soluble dissociated cell wall
component may be separated from the dissociated cells.
[0013] In accordance with preferred embodiments of the invention, a
method for providing a mixture of cell wall ghosts and cytoplasm is
provided. The method includes subjecting the cells to heat, shear,
and pH under conditions sufficient to rupture the cell walls and to
allow the release of cytoplasm therefrom while leaving a
substantially intact cell wall ghost. The method most preferably
comprises jet cooking the cells. In the most highly preferred
embodiments of the invention, the cells are jet cooked to form an
intermediate product, and the intermediate product is subsequently
jet cooked to form the mixture of cytoplasm and cells. The mixture
thus formed may be spray dried or otherwise treated, such as by
substantially separating the cell walls from the cytoplasm. An
animal feed may be prepared from the mixture or spray dried mixture
thus formed.
BRIEF DESCRIPTION OF THE FIGURE
[0014] The FIGURE is a schematic illustration of a yeast cell wall
dissociation method.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0015] The following paragraphs will focus primarily on the
dissociation of yeast cells, but it should be understood that the
invention is not limited thereto. Indeed, the invention is deemed
to be applicable to any prokaryotic or eukaryotic cells, in
particular microbial cells, and especially to yeasts. Other cells
suitable for dissociation in connection with the present inventive
method include fungi, plant cells, spores, and like microorganisms.
More generally, any cell that can be "harvested" to provide
nutrients or other chemically useful materials can be used in
conjunction with the invention. If yeast is used, the yeast is
preferably a strain of Saccharomyces cereviasiae, including those
strains commercially sold as brewer's yeasts and baker's yeasts.
The cells may be alive or dead, or mixtures of live and dead cells
may be employed. The yeast cells may be used as supplied from a
commercial distilling operation, or may be washed prior to use in
conjunction with the invention to remove bittering agents,
fermentation insolubles, and the like. It is contemplated that the
yeast may include fiber carbohydrate, or other material from a
commercial ethanol distilling operation, and in some embodiments of
the invention the yeast source may comprise stillage. A preferred
yeast source is spray dried yeast.
[0016] In accordance with the invention, the walls of cells are
dissociated to yield cell wall components. The dissociation
contemplates a wide range of dissociation of the cell walls, and
the extent of dissociation may be selected by one of skill in the
art. For instance, the cells as received may contain impurities or
non-native components that are bound via electrostatic forces (or
even covalent bonds) to the cell walls. The dissociation in some
embodiments of the invention contemplates removal of these
impurities or non-native components. In preferred embodiments of
the invention, the cell walls are partially disintegrated, such
that some native cell wall components have been liberated from the
molecular structure of the cell walls, but that the cell wall
ghosts are still discernable as discrete entities under microscopic
examination. It is thus contemplated that the ghosts may not be
complete cell walls, inasmuch as some of the original components of
the cell wall may have become dissociated from the remaining
components of the cell wall. Any portion of native cell wall
components may be so liberated, such as 10%, 20%, 30%, 40%, 50%,
60%, 70%, 80%, or 90%, whereby in such embodiments, the cell wall
ghosts are still discernable. In less preferred embodiments of the
invention, the dissociation is completed to an extent such that the
cell walls are substantially completely or fully disintegrated,
such that the cell walls are not visible as discrete entities under
microscopic examination.
[0017] Generally, in accordance with the preferred embodiments of
the invention, the method for rupturing cells comprises subjecting
the cells to heat, pH, and shear under conditions sufficient to
rupture the walls of at least some of the plurality of the cells to
allow cytoplasm to be released therefrom, thereby forming a mixture
of ghosts and cytoplasm. The mechanism of action of the present
invention is believed to be non-specific degradation or of the
cells, whereby oligosaccharides (such as mannanoligosaccharides)
and glucans are released. Upon such degradation, the walls of the
cells weaken eventually to the point of cell wall rupture to
thereby release the cytoplasm contained therein. It is contemplated
that conditions of temperature, pH, shear, and residence time in a
suitable apparatus will vary widely from species to species of the
cell and will further vary depending upon the apparatus chosen.
Generally, it is contemplated that the temperature employed will be
in a range of from 140.degree. to 160.degree. C.
[0018] To hydrolyze the cell walls, a slurry of the yeast may be
prepared by known techniques, such as evaporation or known
liquid-solid separation techniques, or alternatively the yeast may
be dried and subsequently mixed with water to form a slurry. The
solids content of the starting yeast slurry is preferably about 5
to 25% (w/v), preferably 10 to 20%, and more preferably 12 to 18%.
It is desired to employ the solids content as high as is
practicable, and an upper limit of 18 to 20% is deemed most
commercially practicable.
[0019] In carrying out the inventive method, the pH of the slurry
of yeast is adjusted to any suitable pH, preferably a pH between
8.0 and 12.0, more preferably 9.0 to 11.0, and most preferably 9.5
to 10.0, using an alkali agent, most preferably a food-grade alkali
such as sodium hydroxide, calcium hydroxide, or potassium
hydroxide. The invention is not limited to processing under
alkaline conditions. In some embodiments, strongly acidic
conditions, preferably pH 0.5 to 3, and more preferably pH 1 to 2,
may be employed. The preferred acidifying agent is a food-grade
acid, such as hydrochloric, phosphoric, sulfuric, or mixtures
thereof. Because it is believed in most instances that an acid pH
is far more aggressive than the relatively mild alkaline conditions
that may be employed for alkali hydrolysis of the yeast, alkaline
conditions are preferred in connection with the present
invention.
[0020] The alkaline slurry of yeast is then subjected to shearing
under conditions sufficient to rupture the walls of at least some
of the plurality of the yeast cells to thereby release the
cytoplasm. Generally, the cells may be subjected to a pressure of
between 35 to 105 psig at the conditions of temperature, pH, and
shear heretofore discussed. The cells are preferably subjected to
such pressure for a time ranging from 10 to 150 seconds. Once
again, this parameter will be expected to vary with the other
operating parameters.
[0021] Any suitable apparatus may be employed in connection with
the invention. In accordance with highly preferred embodiments of
the invention, a jet cooking apparatus is employed. A jet cooking
apparatus resembles a jet pump that is employed to move liquids and
slurries. In the jet cooking process, high pressure saturated
steam, at a pressure that ranges from about 60 to 200 psig, is
injected through a nozzle into the center of a venturi mix
combining tube. The slurry is then pulled into the annular gap
formed by the steam nozzle and the venturi opening. The slurry is
heated as it accelerates to sonic velocity within the mixing tube.
While passing through the mixing tube, the cells are subjected to
extremely turbulent conditions which cause partial hydrolysis of
the cell walls.
[0022] It is contemplated in preferred embodiments of the invention
that multiple passes through a jet cooking apparatus, preferably
between 2 to 5 passes, and more preferably 2 to 3 passes, will be
employed. If it is desired to completely liquefy the cells, i.e.,
to disassociate the cells to an extent such that the cell walls are
substantially completely dissociated with no intact ghosts
remaining, a higher number of passes, such as 3 to 7, may be
employed. The precise number of passes required to achieve complete
dissociation and the number of passes required to achieve a mixture
of cytoplasm and ghosts will depend upon the specific apparatus
employed and on the other operating conditions.
[0023] Generally, it is believed that the more aggressive
conditions that are employed, such as higher alkalinity and
temperature, the fewer the number of passes will be needed to
liquefy greater than 90% of the cells. The pH of the slurry will
decline after each pass through the jet cooking apparatus, at least
because of the introduction of additional water via the steam
injector, and possibly because of hydroxyl uptake. It is
contemplated that additional alkaline agents may be added after
each pass, but preferably no such agents are added.
[0024] The jet cooking may be practiced as a batch process or as a
continuous process. In either event, the intermediate product
formed upon the first jet cooking pass is preferably held for a
retention time ranging from 30 seconds to 1 hour. Most preferably,
the intermediate product is held at a temperature of 140.degree. to
160.degree. C. and a pressure of 50 to 80 psig, then flashed to
atmospheric pressure before the second or subsequent jet cooking
pass. After the final jet cooking step, preferably there is no
retention period, although such may optionally be employed. If the
product is jet cooked over more than two passes, the intermediate
products prepared after the first pass but before the final pass
may be held for a retention period, or the retention period may be
omitted.
[0025] In accordance with some embodiments of the invention, a
mild, one- or two-pass slightly alkaline pretreatment can be
employed to slightly dissociate the cells. After such pretreatment,
the alkaline liquid can then be removed, and a slurry of cells
formed by adding water. The cell slurry then may be adjusted to the
acidic or alkaline conditions heretofore discussed, and the slurry
then may be jet cooked. It is contemplated that the mild alkaline
pretreatment will remove contaminating biomolecules, small
metabolites, and related fermentation broth products that may
contribute off-flavors or colors or may otherwise negatively affect
the hydrolyzed cells.
[0026] The mixture of cytoplasm and ghosts thus formed is itself
deemed to be a commercially valuable product. It is believed that
this mixture typically will have a solids content that ranges from
about 17 to 20%, with about 35% of the solids content comprising
insoluble materials and the rest comprising soluble materials. The
product mixture thus formed may be treated in any manner desired.
For instance, the soluble portion of the material may be at least
substantially separated from the insoluble portion, such as by
centrifugation. The solids material will comprise largely cell wall
ghosts, and the cell wall ghosts may be sold commercially. The
liquid fraction may be further treated, for instance, by spray
drying the liquid fraction with a suitable carrier. In some
embodiments of the invention, the mixture exiting the jet cooker
may itself be spray dried, with or without a carrier. Any suitable
spray drying carrier may be employed in connection with the
invention, such as maltodextrins, reduced maltodextrins, starches,
starch hydrolyzates, and so forth.
[0027] The invention contemplates a method for feeding an animal,
the method comprising feeding the animal a product mixture prepared
in accordance with the foregoing teachings. The animal also may be
fed a fraction of the mixture heretofore described, for instance,
the solids fraction or the liquid fraction that remains after
centrifuging the product mixture. Generally, the animal will be fed
an animal feed, which includes the mixture heretofore described (or
a suitable fraction thereof) in combination with one or more animal
nutritive sources. The mixture or fraction prepared in accordance
with the present invention may be added in any amount relative to
the other components of the animal feed. Preferably, the mixture or
fraction is added in an amount that ranges from 0.01 to 25% by
weight, although a greater or lesser range is also contemplated.
The invention is deemed to find particular applicability in feeds
for swine, ruminants, poultry, and household pets such as cats and
dogs, although it is contemplated that the invention may find
utility in connection with feeds for other animals. In some
embodiments of the invention, the mixture prepared in accordance
with the foregoing teachings, or a fraction of such mixture, may be
used in connection with human food products. It is believed that
the cytoplasm will provide nutritive benefit to swine and
ruminants, and, surprisingly, it was found in one experiment that
swine prefer food products prepared in accordance with the
foregoing teachings to similar food products prepared with a
commercially available yeast derivative.
[0028] The present invention is deemed to allow the hydrolysis of
cell walls without the need for mechanical, autolytic, or
hydrolytic procedures. Nonetheless, in some embodiments of the
invention, autolysis or hydrolysis procedures may be employed in
conjunction with the procedures heretofore described. In such
cases, it is contemplated that the dissociation afforded by the
invention may decrease incubation time, and/or may improve
enzymatic hydrolysis. Although it is not intended to limit the
invention to a particular theory of operation, it is believed that
such other procedures may so operate by exposing additional
proteins, lipids, or carbohydrates on the cell surface. For similar
reasons, the dissociation afforded by the invention may be used in
conjunction with acid or alkaline hydrolysis procedures by
weakening the cell wall prior to such processing.
[0029] The invention contemplates the selection of conditions of
temperature, pH, and shear to achieve the results desired. By
selection of appropriate conditions, the manner of cell dissolution
may be controlled with precision. For instance, if desired,
dissociation of the cell wall and release of cytoplasmic components
without extensive denaturation of the constituent biomolecules may
be achieved. Alternatively, if more rigorous conditions are
employed, the cell walls may be dissociated to an extent whereby
only the robust soluble or insoluble molecules, such as
alkali-insoluble betaglucans, chitin and the like, remain after
processing. In some embodiments, the invention may be employed to
dissociate cell walls and to harvest oligosaccharides that are
obtained therefrom, with or without rupture of the cell walls
[0030] The following Examples are provided to illustrate the
invention but should not be construed as limiting the scope of the
invention.
Example 1
[0031] This Example illustrates the jet cooking of dried yeast
cells in a skid-mounted jet cooking pilot scale apparatus.
[0032] About 1.8 kg of commercial spray-dried dead Brewer's yeast
was added to about 10 L of cold water with agitation in a mixing
tank. After about 5 minutes an additional quantity of water was
added to bring the final volume to about 12 L. The slurry was
allowed to mix for another 3 to 5 minutes at which time about 500
ml of about 20% concentrated sodium hydroxide was slowly added to
the yeast slurry. The agitation was adjusted to high speed mixing
during and immediately following the alkaline addition. The
moisture was allowed to mix at the high speed for another 5 to 10
minutes whereupon the pH was checked. The measurement showed that
the pH had increased to about 9.2. Another small addition of 20%
sodium hydroxide was used to increase the pH to about 9.7. The
slurry was allowed to mix for another 3 minutes or so at a high
rate of speed at which time the agitation was reduced.
[0033] The mixing tank, which was an integral component of the skid
mounted jet cooker assembly, was connected to a jet cooker by a
valve and piping. At the appropriate time the valve was opened and
the slurry pumped to the cooker. The cooker was calibrated at
320.degree. F. After a residence time in the jet cooker of about 3
minutes, the slurry exited the cooker and was collected (Pass 1).
After most of the final material had entered the cooker piping, and
the mixing tank emptied, the intermediate product thus formed was
transferred to the mixing tank and pumped through the cooker again
(Pass 2). The sample was then collected as it exited the assembly
and set aside to cool.
[0034] The mixture thus formed demonstrated clear microscopic
confirmation of cell dissociation as evidenced by the presence of
cells wall ghosts. After the first pass through the jet cooker,
about 10 to 20% of such cell wall ghosts were observed. After the
second pass, approximately 60 to 70% of the cells typically
appeared as ghosts.
[0035] Some attributes of the processed material are shown in the
following table. In this table, reported viscosity was measured
using a Brookfield viscometer at room temperature (spindle nos. 1,
2, 3, and 5 were used for the respective samples).
TABLE-US-00001 Sample PH Viscosity Yeast Slurry 4.3 38 cP Adjusted
Slurry 10.0 177 cP Jet Cooked Intermediate 9.1 633 cP Product Final
Jet Cooked Mixture 8.0 2230 cP
This data suggests that the rupture of the dead yeast cells is
accompanied by a concomitant change in viscosity (increase) and pH
(decrease). These changes are interpreted as signaling the pasting
and deterioration of the cell wall, and associated release of wall
components such as glucans and oligosaccharides. The release of
glucans and oligosaccharides was believed to be responsible for the
increase in viscosity.
Example 2
[0036] A post-distillation fermentation broth from an ethanol
production plant was centrifuged and the solids recovered as a
slurry. This slurry was composed of about 20% solids which included
primarily (80 to 90%) dead Brewer's yeast cells. The slurry was
spray-dried in a pilot plant dryer and stored at room temperature.
This material was later retrieved from storage and processed
employing the general parameters and multiple pass jet cook
procedures outlined in Example 1 and illustrated in FIG. 1 using
the skid mounted laboratory/pilot plant jet cooking apparatus.
[0037] The observations and results of this experiment were
consistent with other experiments performed in this manner.
Specifically, some (10-20%) dead yeast cell wall dissociation, an
increase in viscosity, and a decrease in pH were observed in the
first jet cooker pass. Immediately following the first pass of the
entire sample volume, this material was transferred back to the jet
cooker feed tank and cycled through again. After the second pass,
the viscosity increased dramatically, the pH declined further and a
significant number of the yeast cells appeared as distended or
swollen cell walls. Cell debris which were not particularly evident
in the unprocessed sample or the first pass material were also
clearly evident.
Example 3
[0038] This example illustrates the purification of fungal chitin
using the method of the invention and a substantially uniform
microbial fungal source.
[0039] A fungal biomass such as Aspergillus niger or Aspergillus
oryzae is concentrated (or dewatered) using a known procedure such
as evaporation, centrifugation and the like to about 12 to 17'%
solids. The pH of the slurry is adjusted to about pH 11 to 12 with
about 5 to 10% sodium hydroxide. The slurry is then jet cooked at
320.degree. F., 50 to 60 psi. The first pass is collected and the
pH readjusted to 11 to 12, as needed. This material is then
subjected to as many jet cook cycles at the strongly alkaline pH as
required to effect hydrolysis of as much of the protein, lipids,
glucan and other biomolecules as possible. The treated material is
next filtered using vacuum filtration or a related procedure to
remove denatured biomolecules and undesirable materials. The
filtered (or alkali insoluble) material is washed with water, the
pH is adjusted and available for use as a substrate for the
production of glucosamine and the like.
Example 4
[0040] Several thousand pounds of dead brewer's dried yeast
obtained from a commercial ethanol distilling operation were
treated in accordance with the present invention to prepare
mixtures of cell wall ghosts and cytoplasm. To prepare the
mixtures, the following procedures were employed.
[0041] A 17% yeast slurry was prepared by adding dried dead yeast
to water with agitation. After about 10 to 20 minutes of aggressive
agitation, the pH of the mixture was adjusted to a pH in the range
of 9.5 to 10.0 with 50% NaOH. Two jet cookers were allowed to
attain temperatures of about 300.degree. F. The jet cookers were
arranged in an in-line configuration.
[0042] The yeast slurry was fed into the primary jet cooker at a
rate of about 1.5 gal/min. The output for this cooker was held for
12 to 15 min. at a temperature of about 150.degree. C. and a
pressure of 50 to 80 psig, flashed to ambient pressure, then fed
directly into the second jet cooker. The jet cooking operations
were conducted to maintain a constant flow from the primary to the
secondary jet cooker. The output from the second jet cooker was
then collected in a holding vessel. After cooling to a temperature
of about 60.degree. to 70.degree. C., the pH ofthe collected
material was lowered from about pH 7 to about pH 4.0 with
hydrochloric acid.
[0043] A preservative (sodium benzoate) was then added in an amount
of 0.8% by weight to minimize microbial growth during transport and
storage to a spray drying facility. Approximately 40 to 50 hours
after jet cooking was completed, the product mixture of cell wall
ghosts and cytoplasm was viscous but still fluid product. This
product was spray dried in a box dryer. No additional carrier was
employed. The spray dried material was evaluated and found to have
a moisture content of about 5%.
[0044] The spray dried mixture was collected and packaged in 50 lb.
paper bags. Several hundred such bags were prepared and were stored
at room temperature.
[0045] Samples of the jet cooked material (before spray drying)
were collected throughout the duration of the run and viewed
microscopically. Both these cooked and those prepared in accordance
with the laboratory procedure of Example 1 exhibited substantially
identical morphology. It was found that 80 to 90% of the cells had
been ruptured to yield cell wall ghosts. These ghosts were observed
to exhibit evidence of cell wall disruption, including distension,
loss of rigidity, non uniformity of size and shape, and so
forth.
Example 5
[0046] The spray dried mixture prepared in accordance with Example
4 was analyzed to yield the following approximate composition.
Whole uncooked yeast was also analyzed. It is seen that a portion
of the nutritive material in the yeast remained substantially
unaffected by the jet cooking process, and that the jet-cooked
mixture could provide nutritive benefit.
TABLE-US-00002 Dried Yeast Jet cooke (Whole) mixture Protein 45.8
44.57 Fiber, Crude 3.6 2.9 Ash 4.5 9.22 Fiber, Dietary, 20.4 19.7
Total Try 0.48 0.48 Cys 0.46 0.33 Met 0.69 0.48 Asp 4.56 5.97 Thr
2.11 2.2 Ser 2.25 2.25 Glu 6.83 5.77 Pro 2.32 2.48 Gly 1.95 1.87
Ala 3.45 2.98 Val 2.45 2.48 Iso 2.09 1.99 Leu 4.03 3.84 Tyr 1.54
1.58 Phe 2.15 2.02 Lys 2.61 2.13 His 0.96 0.96 Arg 1.97 1.44 Vit. A
9,350 5,800 Vit B1 7.62 2.78 Vit. B2 11.8 6.8 Vit. B6 1.56 1.15
Vit. B12 <.002 0.0039 Vit. E <3.0 <3.0 Ca 0.027 0.08 Mg
0.16 0.21 P 0.84 1.06 K 0.68 0.83 Na 0.12 2.35 Cu <.0002 0.00051
Fe 0.0034 0.006 Mn 10 9.6 Zn 56 46
Example 6
[0047] Two commercial swine feed formulations, designated herein as
formulations A and B, were obtained. The spray dried yeast mixture
prepared in accordance with Example 4 was added to each of the
commercial animal feed formulations to form modified formulations
A1 and B1. For comparison, a commercial yeast derivative was also
added to each of the two commercial swine feeds to form modified
formulations A2 and B2. The commercial yeast derivative product was
composed of cell wall ghosts believed to have been prepared by
autolysis, in combination with fermentation solubles. The
commercial yeast derivative was added to the two commercial animal
feeds in an amount of 4 lbs. per ton, whereas the spray dried
product prepared in accordance with Example 4 was added in an
amount of 6 lbs. per ton to achieve a comparable loading of cell
wall ghosts.
[0048] The modified feed formulations A1 and B1 (representing feeds
prepared in accordance with the invention) and A2, and B2
(representing the comparative product) were fed to 100 pigs. The
pigs were housed in ten separate pens, with ten pigs per pen. Each
pen was provided with two feeders. The modified feed formulations
A1 and A2 each were added to one of the feeders, and the amount of
feed consumed by the pigs was measured after three days and after
six days. The feeders were switched one time per day in an effort
to eliminate any bias that may have been associated with the
position of the feeder in the pen. In a separate experiment, the
modified feed formulations B1 and B2 were added to the feeders, and
the amount of feed consumed by the pigs was measured. The following
results were observed.
TABLE-US-00003 B1 A1 Days Lb/Pig % Lb/Pig % P-Value 0-3 .23 33 .46
67 <.01 0-6 .35 18 1.60 82 <.01 B2 A2 Days Lb/Pig % Lb/Pig %
P-Value 0-3 .12 26 .34 74 <.01 0-6 .23 16 1.22 84 <.01
[0049] Surprisingly, for both commercial swine feeds, the pigs
exhibited a strong preference for the modified feed formulated with
the product of Example 4 relative to the commercial cell wall
product. This preference was manifest after three days and became
more pronounced after six days. These results demonstrate that the
pigs exhibited a strong preference for the feed that contained the
material of Example 4. The improved palatability of this feed was
seen to enhance feed uptake.
[0050] It is thus seen that the invention provides a method for
dissociation of cells.
[0051] All references cited herein are hereby incorporated by
reference. All methods described herein can be performed in any
suitable order unless otherwise indicated herein or otherwise
clearly contradicted by context. The use of any and all examples,
or exemplary language provided herein, is intended merely to better
illuminate the invention and does not pose a limitation on the
scope of the invention unless otherwise claimed. No language in the
specification should be construed as indicating any non-claimed
element as essential to the practice of the invention.
[0052] Preferred embodiments of this invention are described
herein, including the best mode known to the inventors for carrying
out the invention. Variations of those preferred embodiments may
become apparent to those of ordinary skill in the art upon reading
the foregoing description. Accordingly, this invention includes all
modifications and equivalents of the subject matter recited in the
claims appended hereto as permitted by applicable law. Moreover,
any combination of the above-descried elements in all possible
variations thereof is encompassed by the invention unless otherwise
indicated herein or otherwise clearly contradicted by context.
* * * * *