Methods and apparatus for producing partially hydrolysed proteinaceous products

• US 20100196538A1
• Filed: 12/04/2009
• Published: 08/05/2010
• Est. Priority Date: 12/04/2008
• Status: Active Grant

• Current Assignee: Axiom Scientific And Charitable Institute, Ltd.
• Original Assignee: Axiom Scientific And Charitable Institute, Ltd.
• Inventors: Law, Roger W.
• Granted Patent: US 8,591,971 B2
• Time in Patent Office: Days
• US Class Current: 426/59
• CPC Class Codes: A23J 3/341 of animal proteins
• CPC Class Codes: C12Y 304/22002 Papain (3.4.22.2)

Abstract

Methods and apparatus for producing a particulate proteinaceous product are disclosed. Raw animal matter comminuted. Hydrolysing enzymes are added to preheated food-grade oil and added to the ground matter. The resulting suspension is preheated to hydrolysis temperature. Controlled hydrolysis of proteins in the suspension achieves a predetermined partial hydrolysis of the proteins to form a hydrolysate/oil suspension. At the desired level of hydrolysis the enzymes are heat-inactivated. Non-digestible solids are removed from the suspension and the suspension is pasteurized and partially dehydrated to concentrate the hydrolysate. Some of the oil is removed to form the product. The method and apparatus exhibit substantial resistance to equipment clogging.

Claims

1. A method for preparing a proteinaceous product from raw protein-comprising animal matter, the method comprising:

(a) providing the raw animal in a ground condition;

(b) adding preheated food grade oil to form an animal matter/oil suspension;

(c) hydrolysing the proteins in the animal matter/oil suspension using proteolytic enzymes, where the hydrolysis is performed at a temperature within a range conducive for hydrolytic activity of the enzymes without denaturing the protein and for a time period sufficient to achieve a preselected degree of partial hydrolysis of the protein, to form a hydrolysate/oil suspension;

(d) heating the hydrolysate/oil suspension sufficiently to deactivate the proteolytic enzymes;

(e) removing at least some non-digestible solids from the hydrolysate/oil suspension;

(f) pasteurizing the hydrolysate/oil suspension;

(g) reducing the concentration of water in the suspension; and

(h) removing a portion of the oil from the suspension to form a particulate, partially hydrolysed, non-denatured proteinaceous product.

2. The method of claim 1, wherein step (a) comprises comminuting the raw animal matter.

3. The method of claim 1, wherein step (b) further comprises adding extraneous hydrolytic enzymes to the oil before adding the oil to the animal matter.

4. The method of claim 3, further comprising pre-heating the food-grade oil.

5. The method of claim 1, further comprising preheating the ground animal matter after step (a) but before step (c) to elevate the temperature thereof to within range conducive for hydrolytic activity of the enzymes without causing denaturation of the protein.

6. The method of claim 5, wherein the ground animal matter is preheated to a temperature within the range of about 140°

F. to 150°

F.

7. The method of claim 5, wherein the ground animal matter is preheated concurrently with the adding of supplementary proteolytic enzymes and food grade oil at step (b).

8. The method of claim 7, wherein the supplementary proteolytic enzymes and food grade oil added at step (b) are preheated to a temperature within the range of about 140°

F. to 150°

F.

9. The method of claim 7, wherein the animal matter/oil suspension is preheated by passing the ground animal matter through a heat exchanger.

10. The method of claim 9, wherein the heat exchanger is a hybrid shell and tube heat exchanger with no moving parts.

11. The method of claim 9, wherein step (c) comprises passing the preheated animal matter/oil suspension through at least one digester in which the proteolytic enzymes partially hydrolyse the proteins in the ground animal matter.

12. The method of claim 11, wherein both preheating the animal matter/oil suspension and step (c) are performed in the heat exchanger.

13. The method of claim 11, wherein the preselected degree of partial protein hydrolysis is achieved by passing the preheated animal matter/oil/enzyme suspension through the at least one digester at a controlled flow-rate in a plug-flow manner.

14. The method of claim 1, wherein in step (d) the hydrolysate/oil suspension is heated to a temperature within a range of about 174°

F. to about 200°

F. to deactivate the enzymes.

15. The method of claim 14, wherein the enzymes are deactivated by injecting steam into the hydrolysate/oil suspension.

16. The method of claim 14, wherein the enzymes are deactivated by passing the hydrolysate/oil suspension through a heat exchanger.

17. The method of claim 1, wherein step (e) is performed using a centrifuge.

18. The method of claim 1, wherein in step (b) the heated food grade oil comprises a portion of the oil removed in step (h).

19. The method of claim 1, wherein step (g) is performed using multi-effect evaporators.

20. A particulate proteinaceous product, prepared by the method recited in claim 1.

21. A method for preparing a particulate proteinaceous product comprising partially hydrolysed animal protein from raw animal matter, the method comprising:

reducing raw animal matter to a ground condition;

adding a preheated food grade oil-enzyme mixture comprising at least one type of proteolytic enzyme to the ground animal matter to form a pre-digestion mixture;

preheating the pre-digestion mixture to a digestion temperature within a range suitable for proteolytic activity or the enzyme composition without denaturing the protein in the pre-digestion mixture;

maintaining the mixture at said digestion temperature while the enzyme partially hydrolyses the proteins in the mixture, to form a hydrolysate/oil suspension;

heat-inactivating the enzymes;

separating and removing solids from the hydrolysate/oil suspension;

removing at least some water from the suspension; and

removing at least some oil from the suspension until the concentration of remaining oil is within a range of about 20 to 35 w/w percent and the concentration of partially hydrolysed animal protein in said product is within a range of about 45 to about 65 w/w percent.

22. A particulate proteinaceous product, prepared by the method recited in claim 21.

23. An apparatus for preparing a particulate, proteinaceous product from raw, protein-comprising animal matter, comprising:

a muller operable to comminute the raw animal matter;

an oil-addition device located downstream of the muller, the oil-addition device being operable to add a mixture of proteolytic enzymes in preheated food-grade oil to the comminuted animal matter;

a heater-hydrolyser located downstream of the muller, the heater-hydrolyser being operable to heat the animal matter/oil/enzyme suspension to a preselected hydrolysis temperature and to allow the preheated suspension to undergo a preselected degree of hydrolysis by the enzymes;

a separator located downstream of the heater-hydrolyser, the separator being configured to remove at least some non-digested solids from the hydrolysate/oil suspension;

a concentrator located downstream of the separator, the concentrator being configured to remove at least some water from the hydrolysate/oil suspension; and

an oil-remover located downstream of the concentrator, the oil-remover being configured to remove at least some oil from the hydrolysate/oil suspension.

24. An apparatus for preparing a particulate, proteinaceous product from raw animal matter, comprising:

comminuting means for comminuting the animal matter;

oil-heater means for preheating food-grade oil;

enzyme-addition means for adding proteolytic enzymes to the food-grade oil and for adding the resulting mixture to the comminuted animal matter;

preheat means for heating the suspension of animal matter/oil/enzymes to a hydrolysis temperature;

hydrolysis means for achieving a predetermined degree of hydrolysis of proteins in the animal matter/oil/enzyme suspension;

separator means for removing non-digestible solids from the hydrolysate/oil suspension;

evaporator means for removing a predetermined amount of water from the hydrolysate/oil suspension; and

oil-removal means for removing a predetermined amount of oil from the hydrolysate/oil suspension to convert the suspension to a particulate proteinaceous product.