Production of liquid foods without off-flavors

Food or edible material: processes – compositions – and products – Processes – Separating a starting material into plural different...

Reexamination Certificate

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C426S488000, C426S634000, C426S518000

Reexamination Certificate

active

06805892

ABSTRACT:

FIELD OF INVENTION
The invention resides in the field of continuous production of liquid food products from a variety of solid foods such as plant seeds, legumes, etc., which liquid food products contain no substantial objectionable off-flavor volatiles.
BACKGROUND OF INVENTION
To be generally acceptable, the foods need not only be nutritious, functional and economical but also be attractive in color, aroma, taste and texture. Plant protein preparations mainly from legumes and nuts, like soybeans, have unacceptable off-flavor volatiles and score heavily against their positive properties and limit their use. Lipoxygenase enzyme has been recognized as the major cause of off-flavor volatiles in most vegetable protein sources including soybeans, peas and peanuts. Extraction of soymilk from soybeans, for example, involves grinding of soybeans in water. The lipoxygenase enzymes released from soybean catalyses reactions among water, oxygen and lipids. Some of the reaction products give off strong beany off-flavor volatiles.
Existing methods deal with the problem of beany off-flavors by thermally and/or chemically inactivating lipoxygenase enzyme in soybeans prior to or during the grinding operation under ambient pressure. For example, because at temperature above 65° C., the half-lives of the various lipoxygenase enzymes rapidly decrease with increasing temperature, heating soybeans above this temperature effectively inactivates lipoxygenase enzyme. Hot grinding of soybeans performs the desired inactivation of the enzyme. Ground soybean slurry can now be further processed without any further problem of off-flavor generation. However, the thermal inactivation of enzyme causes other proteins in soybeans also to prematurely denature and get attached to the fibers in the beans. The extraction of proteins in water thus becomes difficult and leads to reduced yield and chalky mouth-feel. The latter is caused due to fine fibers getting into the liquid extract.
Control of off-flavor volatiles has also been achieved by eliminating available free oxygen under ambient or reduced pressure during the grinding oDeration. The present inventor's earlier U.S. Pat. No. 4,915,972 Apr. 10, 1990 describes a process for preparing protein foods by disintegrating the seeds such as soybeans, peanuts etc., in an oxygen-free environment, thus preventing lipoxygenase enzyme from producing the off-flavor volatiles. This process dispenses with the enzyme inactivation by heat treatment.
Another U.S. Pat. No. 4,744,524 May 17, 1988 by the present inventor describes an equipment which grinds soybeans in an oxygen-free environment. The equipment further cooks and separates the soybean slurry to extract soymilk which has no beany flavor.
U.S. Pat. No. 3,937,843 Feb. 10, 1976 Osaka et al describes bean-odor-free soy bean product and its production. The patent uses lactic fermentation of soy milk.
FIG. 1
illustrates schematically a system for continuously producing soymilks with prior art. Referring to the figure, a rotary valve or auger
10
regulates the feeding of soybeans from a soybean hopper
12
. The soybeans in the hopper may be dry soybeans or may have already been properly soaked. A regulated amount of hot or cold water is added to the soybeans and the mixture is sent to a grinder
14
that grinds soybeans. When hot water is used for grinding and/or steam is injected between the rotary valve
12
and grinder
14
, the lipoxygenase enzyme is partly inactivated and controls beany off-flavor. The hopper
12
may also have water feed and level control for airless feeding and grinding of soybeans. A steam mixer
16
is provided to heat the soybean slurry to a preset temperature. A positive displacement pump (PDP)
18
regulates the slurry flow. A holding tube
20
ensures that the soybeans slurry is properly cooked by maintaining the steam-soybeans slurry mixture at the preset temperatures for a preset duration. A vacuum deodorizer
22
removes the volatiles that may be present in the cooked slurry. A back-pressure valve
24
ensures the maintenance of high pressure and high temperature in the holding tube and a low pressure in the vacuum deodorizer. A PDP
26
sends a regulated amount of cooked slurry to an extractor
28
which separates soymilk and fibrous residue. The extractor can be a centrifugal filter, decanter, filter press, or any other separation device. Soymilk
30
with reduced beany off-flavor volatile is pumped with a PDP
32
for packaging or other processing.
FIG. 2
shows schematically an alternative system similar to that shown in FIG.
1
. In the figure, an extractor
40
is moved upstream so that the slurry is separated into liquid and fibrous residue, and only the liquid is cooked with steam in the steam mixer
42
. The cooked liquid is held under pressure in a holding tube
44
to ensure a proper cooking at a proper temperature before it is led to a vacuum deodorizer
46
.
The methods described thus far for continuously producing non-beany flavor soymilk inactivate the lipoxygenase enzyme thermally or by creating oxygen-free grinding environment. They involve multiple well-controlled steps before soymilk is extracted and ready for further processing. Any departure from the limited range of the operating parameters leads to the degradation of the quality and yield of soymilk. As a result, existing methods are either capital or manpower intensive, and are not easy to adapt to small-scale continuous production with low cost equipment.
SUMMARY OF INVENTION
In accordance with one aspect, the present invention is a process amenable to low cost equipment for making liquid food products with no substantial off-flavor volatiles in a continuous process at a small as well as large scale.
In one aspect, enzymes that produce off-flavor volatiles are instantaneously inactivated thermally concomitantly with or immediately following disintegration of solid food in water while the disintegration is conducted under pressure. The pressurized disintegration permits the temperature of the resulting slurry to be raised to the desired cooking temperature, which is usually about 100° C. or above. Presence or absence of air during disintegration is relatively unimportant.
In another aspect, a system for continuously producing liquid food products with no off-flavor volatiles includes an airless grinder which is operated under pressure so that air leakage is minimized, enabling the use of low cost equipment.
In yet another aspect, the process includes both airless grinding and steam heating operations, which are performed substantially simultaneously under pressure. This simplifies the construction of a system by eliminating some of the components required in the prior art setups.


REFERENCES:
patent: 3937843 (1976-02-01), Osaka et al.
patent: 3982004 (1976-09-01), Obata et al.
patent: 4369198 (1983-01-01), Uchi et al.
patent: 4460613 (1984-07-01), Yang et al.
patent: 4744524 (1988-05-01), Gupta
patent: 4915972 (1990-04-01), Gupta et al.
patent: 5068117 (1991-11-01), McCabe
patent: 6451359 (2002-09-01), Nsofor
patent: 59-140845 (1984-08-01), None
patent: 63-63358 (1988-03-01), None

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