Notes

Snack Food Extruder Machine
A course of as claimed in claim 38 wherein the extract is heated to a temperature of about 285° F and maintained at about 285° F for about 15 seconds to destroy anti-nutritional factors. A course of as claimed in claim 17 wherein the step of neutralizing occurs earlier than the step of clarifying. A course of as claimed in declare 17 whereby the extract is heated to a temperature of about 285° F to destroy anti-nutritional factors. A process as claimed in declare 17 whereby the extract is heated to a temperature of about 285° F and maintained at about 285° F for about 15 seconds to destroy anti-nutritional elements. The extraction solution serves to extract carbohydrates, proteins and lipids, also referred to as fats, from the oilseed. A high temperature, barely acidic, aqueous solution extraction course of for preparing soy milk from dehulled or presoaked beans is described by Wilkens and Hackler in "Cereal Chemistry," July 1969, Volume 46, No. four, P. 391.
Extraction resolution on the price of 4.0 gallons per minute was fed to the Fitz mill. The extraction resolution was prepared by chlorinating 300 gallons of water to 0.01% and adding 1.1 liters of 50% sodium hydroxide to the water. The extraction liquid containing the comminuted soy beans was pumped via 147 ft of two inch stainless steel holding tubing giving about 5 minutes residence time to finish the extraction. This liquid had a ultimate temperature of 195° F and a pH of eight.5. The fact that the product of this course of has high stability during storage is stunning in light of the generally held perception that exposing lipids to a hot alkaline resolution results in saponification of the lipids.
These fat-free flakes are prepared from whole soy beans by dehulling, rolling and hydrocarbon solvent extracting the soy beans. biscuit production line extracted flakes are then steamed and heated to remove traces of solvent. The flakes are normally stored until wanted for extracting the protein.
The launched fat was then extracted utilizing diethyl ether. According to the A.O.C.S. official technique Ba 3-38 petroleum ether extraction methodology the lipid content material of the dried product was solely 4.35% fats. Thus about 80% of the lipids within the product are certain lipids due to encapsulation by protein derivatives. Since certain lipid contents larger than 75% are associated with excessive product stability, this high level of sure lipids indicates that the dried product could be very stable in storage. The dried product is steady for at least 10 months in storage at room temperature.
A course of as claimed in claim 38 comprising the extra step of instantizing the powder. A process as claimed in declare 17 whereby the extraction answer incorporates sodium hydroxide. A course of as claimed in declare 17 comprising the extra step of instantizing the powder. A process as claimed in declare 1 whereby the extraction resolution incorporates sodium hydroxide. A course of as claimed in claim three comprising the additional step of instantizing the powder.
The remainder of the method includes steps for concentrating and stabilizing the extracted carbohydrates, lipids and proteins within the extraction answer. This involves clarifying the neutralized comminuted oilseed/extraction resolution mixture within the clarification stage 14. Clarification can be accomplished before neutralization. A centrifuge is useful for undertaking the clarification step. Sludge, which consists primarily of the fibrous component of the oilseed is the byproduct of the clarification step.
Furthermore, due to the low temperatures of the Chayen course of it is doubtful that lipoxidase and anti-nutritional components similar to anti-trypsin that are in soy beans could be destroyed through the course of. The oxidation reaction takes place quickly each time the bean cell construction is broken as when the bean cotyledons are bruised, cracked or floor, in order that the enzymes and oils are permitted to contact one another. A process as claimed in claim 38 comprising the additional steps of concentrating and spray drying the extract to yield a dry powder. A process as claimed in claim 17 comprising the extra steps of concentrating and spray drying the extract to yield a dry powder. A course of as claimed in claim 1 comprising the extra steps of concentrating and spray drying the extract to yield a dry powder. The lipid content material was decided by disintegrating nonfat portions of the sample with hydrochloric acid within the presence of alcohol as a wetting agent to launch the fats.
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