Notes

Snack Meals Extruder Machine
If needed, the clear extract from the clarification stage 14 could be fed to the heating stage 16 to destroy any anti-nutritional elements which were not destroyed by the extraction solution. This is effected by sustaining the clear extract at a sufficiently high temperature for a adequate time to destroy anti-nutritional factors. Generally the higher the temperature used, the much less residence time required in the heating stage.
The mill was operated with a # IA screen, at an influence forward position. Extraction resolution at the rate of four.zero gallons per minute was fed to the Fitz mill. The extraction answer was prepared by chlorinating 300 gallons of water to zero.01% and adding 1.1 liters of 50% sodium hydroxide to the water. The extraction liquid containing the comminuted soy beans was pumped by way of 147 toes of 2 inch chrome steel holding tubing giving about 5 minutes residence time to complete the extraction. This liquid had a last temperature of 195° F and a pH of eight.5. The incontrovertible fact that the product of this process has high stability throughout storage is surprising in gentle of the generally held belief that exposing lipids to a scorching alkaline solution ends in saponification of the lipids.
Because of those variations of the popular embodiment which are obvious to 1 expert within the art, the spirit and scope of the appended claims should not necesarily be limited to the outline of the preferred embodiment. EXAMPLE 2 Using the process of Example 1, entire shelled peanuts were successfully handled. The yield was 79.3%. The Chayen process does overcome a few of the disadvantages of the hydrocarbon extraction course of. Any residual style from the hydrocarbons is eradicated.
The comminuted oilseed/extraction solution combination is then neutralized with an acidic resolution. Any non-toxic acid could additionally be used. However it's most popular to make use of hydrochloric acid, since it's readily available and inexpensive. The acid answer ought to be thoroughly mixed with the combination to prevent insolubilization of protein.
A course of as claimed in claim 1 whereby the extraction resolution incorporates sodium hydroxide. A process as claimed in claim 3 comprising the extra step of instantizing the powder. If a powder product is desired, the extract could be concentrated and spray dried utilizing standard means to yield a stabilized, full fat, high protein powder. This powder could be instantized utilizing conventional means to improve the powder's dispersibility in aqueous options. biscuit production machine as claimed in claim 38 wherein the step of clarifying includes the step of centrifuging.
As used herein the term "bound lipids" refers to the share of the whole lipids within the product which aren't extracted by conventional petroleum ether methods. Total lipids are determined by acid hydrolyzing the product before conducting the traditional ether extraction. Sufficient extraction solution having a sufficiently excessive pH to yield an alkaline oilseed/extraction answer mixture, i.e., a combination having a pH greater than 7.zero, is offered. Generally, the higher the pH of the extraction solution and thus the oilseed/extract answer mixture, the upper the yields obtained from the oilseed. For example, the yield increases from about sixty one to about 85% because the pH of the oilseed/extraction answer combination is elevated from about 7 to about eleven when soy beans are used as 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 claim 38 whereby the comminuted oilseed/extraction answer combination has a pH from about 8.5 to about 9. A course of as claimed in declare 38 whereby the comminuted oilseed/extraction solution mixture has a pH from about 8 to about 10. A process as claimed in claim 17 wherein the comminuted oilseed/extraction solution combination has a pH less than about eleven. A process as claimed in claim 17 wherein the comminuted oilseed/extraction solution combination has a pH from about 8.5 to about 9. A process as claimed in claim 17 whereby the comminuted oilseed/extraction solution combination has a pH from about 8 to about 10. A course of as claimed in claim 1 whereby the comminuted oilseed/extraction solution combination has a pH from about eight.5 to about 9.
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