Protein hydrolysis

Claim 2

A process for the hydrolysis of protein comprising the steps of: (a) hydrolyzing a selected protein material, dispersed in an aqueous medium together with at least one active proteolytic enzyme component, at a controlled temperature and alkaline pH; (b) separating the hydrolyzed protein material, by filtration employing a molecular weight-selective filter medium, into a lower molecular weight first protein filtrate fraction and a higher molecular weight second protein reject fraction, said second protein reject fraction including substantially all of the active proteolytic enzyme component; (c) recycling at least a portion of the second protein reject fraction to the hydrolysis step; and (d) recovering low molecular weight protein hydrolyzate from the first protein fraction.

Claim 3

The process of claim 1 wherein the selected protein material comprises a protein isolate derived from oil seeds.

Claim 4

The process of claim 2 wherein the selected protein material is a soybean isolate.

Claim 5

The process of claim 1 wherein the aqueous medium contains from about 0.5 to about 4.0 wt. % of selected protein material.

Claim 6

The process of claim 4 wherein the aqueous medium contains from about 1.0 to about 1.5 wt. % of selected protein material.

Claim 7

The process of claim 1 wherein the hydrolysis temperature is maintained within the range from about 25° to about 60° C.

Claim 8

The process of claim 1 wherein the alkaline pH of the hydrolysis medium is maintained within the range from about 7 to about 9.

Claim 9

The process of claim 7 wherein the alkaline pH of the hydrolysis medium is maintained by the controlled addition of a dilute aqueous solution of an alkali or alkaline earth metal hydroxide.

Claim 10

The process of claim 8 wherein the metal hydroxide is sodium hydroxide.

Claim 11

The process of claim 8 wherein the metal hydroxide is calcium hydroxide.

Claim 12

The process of claim 1 wherein the proteolytic enzyme comprises an alkaline protease.

Claim 13

The process of claim 1 wherein the filter medium comprises a hollow-fiber membrane.

Claim 14

The process of claim 12 wherein the hollow-fiber membrane is selected to permit passage into the filtrate of protein hydrolyzate having a molecular weight generally not greater than about 20,000.

Claim 15

The process of claim 13 wherein the hollow-fiber membrane is selected to permit passage into the filtrate of protein hydrolyzate having a molecular weight generally not greater than about 10,000.

Claim 16

The process of claim 1 wherein the first protein filtrate fraction is subjected to filtration successively through a series of selected hollow-fiber membranes to separate a plurality of protein hydrolyzate filtrate fractions characterized by successively lower average molecular weights.

Claim 17

The process of claim 15 wherein the first protein filtrate fraction is separated into a higher average molecular weight protein hydrolyzate fraction and a lower average molecular weight protein hydrolyzate fraction.

Claim 18

The process of claim 1 wherein the second protein reject fraction is subjected to filtration successively through a series of selected hollow-fiber membranes to separate a plurality of protein reject fractions characterized by successively higher average molecular weights.

Claim 19

The process of claim 1 wherein the protein material is first heated to about 100° C. for from about 10 to about 60 minutes and filtered to remove substantially all particles having a diameter greater than about 100 microns.

Claim 20

The process of claim 1 wherein the hydrolysis temperature is maintained within the range from about 25° to about 60° C. and the proteolytic enzyme comprises an alkaline protease.

Claim 21

The process of claim 1 wherein the respective steps are conducted in a continuous manner.

Claim 22

A continuous process for the enzymatic hydrolysis of protein material, comprising the steps of: (a) heating an aqueous slurry of protein material at a temperature within the range from about 90° to about 100° C.; (b) filtering the heated slurry through a filter medium selected to provide an aqueous protein material dispersion whose particles possess no dimension greater than about 100 microns; (c) cooling the filtered aqueous protein material dispersion to a temperature within the range from about 25° to about 60° C.; (d) providing an aqueous dispersion of a proteolytic enzyme material, pretreated by passage through a filter medium, comprising a first hollow-fiber membrane, to remove all components having a molecular weight less than the nominal molecular weight cut-off value of the hollow-fiber membrane; (e) introducing the aqueous protein material dispersion and pretreated proteolytic enzyme into an agitated hydrolysis zone, maintained at a temperature from about 25° to about 60° C., and at a pH from about 7.0 to about 9.0; (f) continuously transferring partially hydrolyzed protein material dispersion to a filtration zone, having a filter medium comprising a second hollow-fiber membrane selected to pass only protein hydrolyzate components having a molecular weight less than the nominal molecular weight cut-off value of the hollow-fiber membrane; (g) filtering the partially hydrolyzed protein material; (h) recovering a low molecular weight protein hydrolyzate f (i) recycling to the hydrolysis zone protein hydrolyzate material having a molecular weight greater than the nominal molecular weight cut-off value of the second hollow-fiber membrane together with the proteolytic enzyme material.

Claim 23

A continuous process for the enzymatic hydrolysis of protein material, comprising the steps of: (a) heating an aqueous slurry of protein material at a temperature within the range from about 90° to about 100° C.; (b) filtering the heated slurry through a filter medium selected to provide an aqueous protein material dispersion whose particles possess no dimension greater than about 100 microns; (c) cooling the filtered aqueous protein material dispersion to a temperature within the range from about 25° to about 60° C.; (d) providing an aqueous dispersion of a proteolytic enzyme material, pretreated by passage through a filter medium, comprising a first hollow-fiber membrane, to remove all components having a molecular weight less than the nominal molecular weight cut-off value of the hollow-fiber membrane; (e) introducing the aqueous protein material dispersion and pretreated proteolytic enzyme into an agitated hydrolysis zone, maintained at a temperature from about 25° to about 60° C., and at a pH from about 7.0 to about 9.0; (f) continuously transferring partially hydrolyzed protein material dispersion to a filtration zone, having a filter medium comprising a second hollow-fiber membrane selected to pass only protein hydrolyzate components having a molecular weight less than the nominal molecular weight cut-off value of the hollow-fiber membrane; (g) filtering the partially hydrolyzed protein material; (h) recovering a low molecular weight protein hydrolyzate f (i) recycling to the hydrolysis zone protein hydrolyzate material having a molecular weight greater than the nominal molecular weight cut-off value of the second hollow-fiber membrane together with the proteolytic enzyme material.

Claim 24

The process of claim 21 wherein the nominal molecular weight cut-off value of the first hollow-fiber membrane is about 10,000.

Claim 25

The process of claim 21 wherein the nominal molecular weight cut-off value of the second hollow-fiber membrane is about 10,000.

Claim 26

The process of claim 21 wherein the protein material is an oilseed protein and the aqueous slurry comprises ground, pressed oilseed.

Claim 27

The process of claim 24 wherein the oilseed protein is soybean protein.