This invention concerns making artificial milk from plant seeds such that the undesirable flavors and taste ar 5 prevented from developing. More specifically, this invention relates to producing no-beany εoymilk without bitterness or chalkiness from soybeans. BACKGROUND OF THE INVENTION

The artificial milk made from soybeans, hereafter 0 called εoymilk, is well recognised to be a highly nutritious, versatile and economical food. However, most methods of making soymilk develop unacceptable off-flavors which greatly limit its use.

Plant protein in legumes and oilseeds, such as 5 cottonseed, peanut, rapeseed, saflower, sesame, soybean and sunflower, is of high enough quality to be almost nutritionally equivalent to the animal protein at a fractio of the cost of the latter. The processing of these seeds t make protein foods having high solubility in water usually 0 leads to flavor and taste problems. Such problems have limited their use mainly for edible oil extraction. The protein rich seed meal remaining after extraction of oil is used essentially as animal feed.

It is well known that certain enzymes present in 5 soybeans and many other seeds are the major cause of off-flavors arising upon processing these seeds for foods. Polyunsaturated fatty acids are catalytically oxidized by the enzymes in the presence of water and oxygen to produce hydroperoxides which finally yield the off-flavor causing 0 volatiles. Lipoxygenase, distributed throughout the soybea cotyledons, becomes active as soon as their cell structure is broken. Therefore, the control of off-flavors has traditionally been done by inactivating the enzyme, such as by heating and/or altering pH of the aqueous medium in whic the seeds are disintegrated. The problem with these treatments has been that they tend to inεolublize the soybean protein and thereby reduce soymilk yield and make i

chalky in outhfeel. The degree of enzyme inactivation required -to reduce the off-flavors to acceptable level lea to an unacceptably low protein solubility. An approach of tackling the problem is to only partially inactivate the

5 enzyme, remove most remaining off-flavor by deodorization, and mask any residual off-flavor by flavoring. In another approach, the enzyme is totally inactivated prior to disintegrating the beans, and the resulting insoluble soybean protein is dispersed in water by fine grinding and

10 high pressure homogenizing. Yet another approach has been to inactivate the enzyme partially by grinding the beans i hot, pH controlled aqueous medium under limiting oxygen condition. Existing methods of making no-beany flavor soymilk are based on the above approaches or a combination

15 of these.

Only recently was it recognized and demonstrated that it is totally unnecessary to inactivate the enzyme, prior or during the disintegration of soybeans, if said disintegration is carried out in an oxygen-free environmen

20 This method has yielded soymilk with absolutely no beany flavor, high degree of dissolved proteins and other soybea solids and no bitterness or throat catching sensation. Employing this method,the present invention describes an equipment to make soymilk, and aqueous extract of other

25 seeds having problems similar to that of soybeans, in commercial as well as small quantities.

DESCRIPTION OF THE PRIOR ART

There are several methods for making palatable produc from seeds containing lipoxygenase and the like enzymes -

30 which cause bad odor, flavor and taste in the end products. Many of these deal with the processing of soybeans. The flavor problems in foods from soybeans have been reviewed J.E.Kinsella and S.Damodaran in a book "The Analysis and Control of Less Desirable Flavors in Foods and Beverages"

35 edited by G.Charalambous and published by Academic Press i 1980. The fact that the enzymes are heat sensitive and ha greatly reduced activity in alkaline as well as acidic

aqueouε media, has been used in many processes for the control of undesirable flavors. Wilkens et al, in an article published in 1967 in Food Technology, Vol.21, p.1630, have described a method of producing nearly bland soymilk by grinding soybean in hotwater having temperatur 80 C or higher and maintaining the resulting slurry at su temperature for 10 minutes or longer to completely inactivate lipoxygenase. Nelson et al, in the US patent 3,901,978 issued on August 26, 1975, have detailed a proc in which steeped soybeans are blanched to inactivate the enzyme before grinding. Wakana et al, in the US patent 4,241,100 issued on December 23, 1980, claimed a process make good tasting εoymilk by boiling unsteeped soybeans i an alkaline aqueous medium for few minutes to inactivate t enzyme before grinding the beans. Uchi and Hatanaka have disclosed in a US patent 4,369,198 issued on January 18, 1983 that soymilk with reduced odor can be made by grindin unsteeped soybeans in deoxygenated hot water from 70 °C to the boiling point under anaerobic condition. There are several variations of the above methods described in the open and patent literature. But exceptin the method of Gupta and Gupta, disclosed for the first tim in the Canadian patent application 477,902 filed on March 29, 1985, all these methods require heat treatment of soybeans prior to or during their disintegration operation or both. Such heat treatment reduces the soymilk yield significantly and imparts chalkiness in the end product. Improving yield by fine grinding the solids and high pressure homogenization causes soymilk to have high degree of suspended particles, which results in increased sensati of chalkiness in the mouth.

Gupta and Gupta realized that if the disintegration o soybeans and other problem seeds is carried out in an environment so low in molecular oxygen that none is available to the reactions catalysed by lipoxygenase to create off-flavor causing volatiles, then there will be no need to inactivate the enzyme at least until after the

disintegration of the seeds. By altogether avoiding heat treatment of seeds prior to or during the disintegration process, they were able to eliminate the concomitant effect of insolubilizing protein in the seeds . Within the scope o

5 this new approach, the present invention describes an equipment that produces soymilk at commercial scale with absolutely no beany flavor.

SUMMARY OF THE INVENTION

The main objective of this invention is to provide an

10 equipment that can be used for the commercial scale production -of artificial milk from soybeans, and aqueous extract of other problem seeds, without the undesirable off-flavors, mouthfeel or bitterness. The equipment eliminates free-oxygen from the seed disintegration

15 environment by carrying out the disitegration entirely in a aqueous medium and preventing completely the access of air to the disintegration region. In some adaptations of the equipment it is possible to pressure cook the resulting see slurry in aqueous medium to the desired temperature and

20 duration under pressure before expelling it from the equipment for further processing.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic drawing of a batch type airless disintegrator cum cooker in accordance with the invention.

25 FIG. 2 is a schematic drawing of a batch type airless disintegrator in accordance with the invention.

FIG..3 is a schematic drawing of a continuous type airless disintegrator in accordance with the invention.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

30 The invention can be shown schematically such as in FIGs. 1, 2 and 3. FIG. 1 depicts an embodiment of the invention in which pressure cooked no-beany flavor aqueous slurry of soybeans and the like problem seeds is the output of the equipment. Steeped or dry beans, adequately cleaned

35 and washed, are put into the equipment with water through hopper 1 by opening a valve 2. The water is made slightly

alkaline such as by adding about 0.05% sodium bicarbonate ordinary drinking or deaerated water, but could also be mad slightly acidic or a solution of a salt. Opening of the valve 4 helps air to escape through the vent tube 3 to allo the beans and water to flow freely into the grinding region 10. A quantity of beans and water sufficient to fill the equipment above the level of valves 2 and 4 is admitted. I the filling process water rises only partially in region 13 through a narrow opening 11 at the bottom of the wall 5 separating the two regions. The opening 11, connecting the region 10 and 13, is made in such a way that there is almos no dynamic coupling of fluids in the two regions, while permitting fluid thermal expansion in region 10. The volum of air trapped in region 13 is large enough, prior to steam infusion heating, that upon being compresεed by condenεed εteam, the pressure in the vessel remains within the safe operating limit of the equipment.

The beans are directed to the hammermill 9 with a preforated hopper 6 which allows the ground beans to pass through it almost uninterrupted. A disc 7 regulates the flow of beans in the hammermill . Screen 8 permits only wel ground beans to leave the hammermill. Circular steam injection pipes 14 and 15 can independently heat the contents of regions 10 and 13. The outer wall 12 of the veεsel is designed to withstand the pressure and temperatur desired for cooking the slurry. The slurry is extracted from the equipment by opening valve 16.

After the equipment is charged with the beans and wate in the desired ratio, and the valves 2 and 4 are closed upo taking care that no air is trapped in region 10, the hammermill motor is started to grind the beans. After the bean grinding is complete, the slurry is cooked by steam infusion to the desired temperature. In an actual commercial operation the steam infusion is begun εimulta- neously with the grinder motor to save time. However, unti the grinding is essentially complete the temperature is not allowed to rise above 60 "C to avoid adversely affecting

the protein solubility of the beans in water. Once the bean grinding is complete, the motor speed may be stepped down. The hammermill now acts as a mixer to generate forced convection in the fluid to heat it evenly. When the slurry is cooked it is expelled from the equipment to a centrifuge or some other device to extract soymilk.

FIG.2 shows an embodiment of the invention in which uncooked no—beany flavor slurry of soybeans and the like seeds is the output of the equipment. This equipment differs from that of FIG.l in that it does not have the outer vessel 12 and the circular steam heating pipes. Also the vent tube is not provided with a valve. The equipment is charged to the level just above valve 2 with the beans and water in the desired ratio, and then valve 2 is closed. The motor is started to grind the beans. The vent tube 3 prevents building up of pressure in the equipment as a result of any increase in volume of the fluid by frictional heating. After all the beans are ground, which may be detected by monitoring current through the grinder motor, the slurry is pumped out either to a εolid-liquid separator to extract soymilk or the like before cooking, or to a cooker.

The above embodiments of the invention are for making soymilk and the like in batch procesεing mode. By taking the output of the grinder in FIG 2 to a balance tank and using a continuous cooker, the production of soymilk and the like can be easily made continuous. Alternatively, two of the above described equipments can be made to operate in parallel such that while one is performing the grinding operation, the other is being emptied for further processing.

In yet another embodiment of the invention, FIG.3, the beans and water in desired ratio are continuously fed to the grinder using a screw conveyor 18 driven by a motor 17, and the slurry is continuously taken out through a valve 16.

Care is taken that air is not εucked into the grinder while

it is operating by providing a mechanism to stop grinder motor if water in the feed hopper 1 falls below a predetermined level.

It is understood that as used herein a) the term "water" includes drinking water, deaerated water, and dilu aqueous solution of an acid, alkali or salt; b) the terms "soybean", "bean" and "seed" include all the seeds which give rise to flavor problem in making aqueous extracts due to the presence of oxygen at the time of disintegrating them; and c) the term "soymilk" includes aqueous extract o the seeds.

Since many apparently widely different embodiments of this invention could be made without departing from the scope and spirit thereof, it iε intended that all matter contained in the above description be interpreted as being illustrative only and not limiting.