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Snack Meals Extruder Machine
It is basically freed from fiber and beany taste. It is dispersible in water and appropriate with whey and different meals materials. When combined with products such as whey, a powder made from soy beans yields a palatable, nutritious milk beverage. It is fascinating to comminute the oilseed to as fine a particle size as potential. The finer the grind of the material the larger the floor space available for extraction and thus the higher the yield of product.
If a product in a powder kind is desired, the clear extract from the cooling stage 18 may be despatched to the focus stage 20 and the spray drying stage 22. When the powder is meant to be used with liquids, it can be instantized within the instantizing stage 24. The extract is then cooled within the cooling stage 18 to stop degradation of the seed materials extracts. The clear extract can be used instantly as product, either alone, or mixed with other liquid sources of nutrients similar to whey.
If essential, the clear extract from the clarification stage 14 may be fed to the heating stage sixteen to destroy any anti-nutritional factors which were not destroyed by the extraction solution. This is effected by sustaining the clear extract at a sufficiently high temperature for a enough time to destroy anti-nutritional factors. Generally the upper the temperature used, the less residence time required within the heating stage.
The most popular equipment for comminution is a hammermill, which has been shown to satisfactorily produce a fantastic grind of oilseed in the presence of the extraction resolution. An added advantage of a hammermill is that it tends to aerate the extraction answer. To overcome the disadvantages of hydrocarbon solvent extraction methods researchers have developed water extraction techniques. Chayen, in U.S.
As used herein the term "certain lipids" refers to the proportion of the entire lipids in the product which aren't extracted by standard petroleum ether strategies. Total lipids are determined by acid hydrolyzing the product earlier than conducting the standard ether extraction. Sufficient extraction solution having a sufficiently excessive pH to yield an alkaline oilseed/extraction answer combination, i.e., a mixture having a pH greater than 7.0, is provided. Generally, the upper the pH of the extraction resolution and thus the oilseed/extract answer combination, the higher the yields obtained from the oilseed. For instance, the yield increases from about sixty one to about 85% because the pH of the oilseed/extraction answer mixture is elevated from about 7 to about eleven when soy beans are used because the oilseed feed. However, at a pH of about eleven of the oilseed/extraction answer combination, the resultant product has a slight sulfide odor.
A course of as claimed in declare 1 wherein the comminuted oilseed/extraction resolution mixture has a pH from about 8 to about 10. A course of as claimed in declare 1 whereby the extract is maintained at about 285° F for about 15 seconds. The clear extract was pumped via Mallory tubes and heated to 285° F for 15 seconds, after which cooled to 140° F.
A excessive temperature, slightly acidic, aqueous resolution extraction course of for preparing soy milk from dehulled or presoaked beans is described by Wilkens and Hackler in "Cereal Chemistry," July 1969, Volume forty six, No. 4, P. 391. BACKGROUND OF THE INVENTION This invention relates to food products, and especially to food merchandise obtainable from oilseeds, as for example, soy beans and peanuts. A process as claimed in claim 38 whereby the hammermill is utilized for comminuting the oilseeds. A course of as claimed in claim 17 wherein a hammermill is utilized for comminuting the oilseeds. biscuit production machine of as claimed in claim 1 whereby a hammermill is utilized for comminuting the oilseeds.
The extracted flakes are then steamed and heated to remove traces of solvent. The flakes are often saved until wanted for extracting the protein. A course of as claimed in declare 38 comprising the extra step of instantizing the powder. biscuit production line of as claimed in declare 17 wherein the extraction solution contains sodium hydroxide. A course of as claimed in declare 17 comprising the additional step of instantizing the powder.
From about 3 to about 15 parts by weight of the hot alkaline extraction solution per part oilseed are used. [newline]If less than about 3 components are used it's discovered that the ensuing slurry is simply too viscous to deal with when soy beans are used because the feed. At ratios larger than about 15 the energy necessities turn into prohibitively costly in concentrating and spray drying the extract. In addition excessive ranges of extraction resolution decrease the yield of the process as a end result of oilseed extracts tend to be discarded with the sludge produced in the clarifying stage. The resultant product must be of good initial flavor and be steady with minimal rancidity and minimal taste improvement in storage.
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