US2011159166A1PendingUtilityA1

Novel canola protein isolate

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Assignee: SCHWEIZER MARTINPriority: Jan 20, 2004Filed: Mar 8, 2011Published: Jun 30, 2011
Est. expiryJan 20, 2024(expired)· nominal 20-yr term from priority
A23J 1/14C07K 14/415A23J 3/14A23J 1/00A23J 3/00
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Claims

Abstract

A novel canola protein isolate consisting predominantly of 2S canola protein and having improved solubility properties, has an increased proportion of 2S canola protein and a decreased proportion of 7S canola protein. The novel canola protein isolate is formed by heat treatment of aqueous supernatant from canola protein micelle formation and precipitation, to effect precipitation of 7S protein which is sedimented and removed. Alternatively, the novel canola protein isolate may be derived from a selective membrane procedure in which an aqueous canola protein solution containing 12S, 7S and 2S canola proteins is subjected to a first selective membrane technique to retain 12S and 7S canola proteins in a retentate, which is dried to provide a canola protein isolate consisting predominantly of 7S canola protein, and to permit 2S canola protein to pass through the membrane, the permeate is subjected to a second selective membrane technique to retain 2S canola protein and to permit low molecular weight contaminants to pass through the membrane, and the retentate from the latter membrane technique is dried.

Claims

exact text as granted — not AI-modified
1 .- 2 . (canceled) 
     
     
         3 . A canola protein isolate consisting predominantly of 2S canola protein having a protein content of at least about 90 wt % (N×6.25) on a dry weight basis, said canola oil protein isolate being derived from a selective membrane procedure in which an aqueous canola protein solution derived from canola oil seed meal and containing 12S, 7S and 2S canola proteins is subjected to a first selective membrane technique which selectively retains 12S and 7S canola proteins in a retentate and permits 2S protein to pass through the membrane as a permeate, the permeate is subjected to a second selective membrane technique which selectively retains 2S canola protein and permits low molecular weight contaminants to pass through the membrane as a permeate, and the retentate from the second selective membrane technique is dried. 
     
     
         4 . The canola protein isolate of  claim 3  having a protein content of at least about 100 wt % (N×6.25) d.b. 
     
     
         5 . A canola protein isolate having a protein content of at least about 90 wt % (N×6.25) on a dry weight basis (d.b.) and containing at least about 85 wt % of 2S canola protein and less than about 15 wt % of 7S canola protein of the canola proteins present in the isolate. 
     
     
         6 . The canola protein isolate of  claim 5  wherein the isolate contains at least about 90 wt % of 2S canola protein and less than about 10 wt % of 7S canola protein of the canola proteins present in the isolate. 
     
     
         7 . The canola protein isolate of  claim 5  having a protein content of at least about 100 wt % (N×6.25) d.b. 
     
     
         8 . A process for the preparation of a canola protein isolate having an increased proportion of 2S canola protein, which comprises:
 (a) providing an aqueous solution of 2S and 7S proteins consisting predominantly of 2S protein,   (b) heat treating the aqueous solution to cause precipitation of 7S canola protein,   (c) removing degraded 7S protein from the aqueous solution, and   (d) recovering a canola protein isolate having a protein content of at least about 90 wt % (N×6.25) d.b. and having an increased proportion of 2S canola protein.   
     
     
         9 . The process of  claim 8  wherein said heat treatment step is effected under temperature and time conditions sufficient to degrade at least about 50 wt % of the 7S canola protein present in said aqueous solution. 
     
     
         10 . The process of  claim 9  wherein said heat treatment step degrades the 7S canola protein by at least 75% of 7S canola protein present in said aqueous solution. 
     
     
         11 . The process of  claim 8  wherein said heat treatment step is effected by heating the aqueous solution for about 5 to about 15 minutes at a temperature of about 75° to about 95° C. 
     
     
         12 . The process of  claim 8  wherein said aqueous solution of 2S and 7S canola proteins is concentrated supernatant from canola protein micelle formation and precipitation. 
     
     
         13 . The process of  claim 12  wherein said canola protein micelle formation is effected by:
 (a) extracting canola oil seed meal at a temperature of at least about 5° C. to cause solubilization of protein in said canola oil seed meal and to form an aqueous protein solution, 
 (b) separating said aqueous protein solution from residual oil seed meal, 
 (c) increasing the concentration of said aqueous protein solution to at least about 200 g/L while maintaining the ionic strength substantially constant by a selective membrane technique to provide a concentrated protein solution, 
 (d) diluting said concentrated protein solution into chilled water having a temperature of below about 15° C. to cause the formation of the protein micelles, and 
 (e) separating supernatant from settled protein micellar mass. 
 
     
     
         14 . The process of  claim 13  wherein said supernatant is concentrated to a protein concentration of about 100 to about 400 g/L prior to said heat treatment. 
     
     
         15 . The process of  claim 14  wherein said supernatant is concentrated to a protein concentration of about 200 to about 300 g/L. 
     
     
         16 . The process of  claim 14  wherein said concentration step is effected by ultrafiltration using membrane having a molecular weight cut-off about 3,000 to about 100,000 daltons. 
     
     
         17 . The process of  claim 16  wherein the concentrated supernatant resulting from ultrafiltration is subjected to diafiltration prior to said heat treatment step. 
     
     
         18 . The process of  claim 17  wherein said diafiltration step is effected using from about 2 to about 20 volumes, preferably about 5 to about 10 volumes, of water using a membrane having a molecular weight cut-off of about 3,000 to about 100,000 daltons. 
     
     
         19 . The process of  claim 8  wherein said canola protein isolate has a protein content of at least about 100 wt % (N×6.25) d.b. 
     
     
         20 .- 26 . (canceled) 
     
     
         27 . An aqueous solution of the canola protein isolate of  claim 5 . 
     
     
         28 . The aqueous solution of  claim 27  which is a canola protein isolate fortified soft-drink. 
     
     
         29 . An aqueous solution of the canola protein isolate of  claim 5 . 
     
     
         30 . The aqueous solution of  claim 29  which is a canola protein isolate-fortified soft drink. 
     
     
         31 . The process of  claim 8  wherein said heat treatment step is effected by heating the aqueous solution for about 2 to about 30 minutes at a temperature of 70° to about 100° C.

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