Burcon Nutrascience (mb) Corp.

Other

Burcon Nutriscience (mb) Corp.

Burcon Mutrascience (mb) Corp.

Burcon Nurtrascience (mb) Corp.

Burcon Nutrascience Corp.

Kevin I Segall

Martin Schweizer

Brent Everett Green

Sarah Medina

Brandy Gosnell

Randy Willardsen

Brent E Green

James Logie

Radka K Milanova

Lei Xu

Johann Tergesen

Edwin Catipon

Russ Sampson

Roland Rosset

Curtis D Hayden

Randy Williardsen

Martin Schwetzer

Martin I Schweizer

The invention relates to a method of processing a pulse protein material, which comprises effecting hydrolysis of the pulse protein material, optionally adjusting the pH, then separating to form a soluble fraction and processing the soluble fraction to provide a pulse protein hydrolyzate which is substantially completely soluble throughout the pH range of about 2 to about 7 and which provides little or no astringency when an acidic beverage containing the pulse protein hydrolyzate is consumed and a solid residue, and processing the solid residue to provide a second pulse protein hydrolyzate having an improved Amino Acid Score, which is improved compared to the substrate pulse protein material.

Preparation of acid soluble pulse protein hydrolyzates with little or no astringency and pulse protein hydrolyzates of improved amino acid score

The present invention is directed to processes for producing pulse protein products, very low in, or substantially free of, pea/vegetable flavour notes useful for the fortification of food and beverage products and prepared without the use of salt in the process. The pulse protein products are obtained by extracting pulse protein source with water to form an aqueous pulse protein solution, at least partially separating the aqueous pulse protein solution from residual pulse protein source, adjusting the pH of the aqueous pulse protein solution to a pH of about 1.5 to about 3.4 to solubilize the bulk of the protein and forming an acidified pulse protein solution then separating the acidified pulse protein solution from the acid insoluble solid material. Also described is the preparation of an acid soluble protein product and which provides acidic solutions of improved clarity and is derived from the acidified pulse protein solution.

Preparation of pulse protein products ('YP810')

A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., is prepared from a soy protein source material by extraction of the soy protein source material with an aqueous calcium salt solution to cause solubilization of soy protein from the protein source and to form an aqueous soy protein solution, separating the aqueous soy protein solution from residual soy protein source, concentrating the aqueous soy protein solution while maintaining the ionic strength substantially constant by using a selective membrane technique, optionally diafiltering the concentrated soy protein solution, and drying the concentrated and optionally diafiltered soy protein solution.

Production of soy protein product using calcium chloride extraction ('S702/S7300/S7200/S7301')

The present invention is directed to soy protein products, very low in, or free of, beany flavour notes and useful for the fortification of food and beverage products and prepared without the use of salt in the process. The soy protein products of the present invention are obtained by extracting soy protein source with water to form an aqueous soy protein solution, at least partially separating the aqueous soy protein solution from residual soy protein source, adjusting the pH of the aqueous soy protein solution to a pH of about 1.5 to about 3.6 to solubilize at least a portion of the protein and form an acidified soy protein solution then separating the acidified soy protein solution from the acid insoluble solid material. The acidified soy protein solution may be dried following optional concentration and diafiltration to form a soy protein product, which may be an isolate. The acid insoluble solid material may be washed with acidified water and then dried to form another soy protein product. These products may be dried at the acidic pH at which they were prepared or may be adjusted in pH before drying.

Preparation of soy protein products (S810)

The present invention is directed to pulse protein products, very low in, or substantially free of, pea/vegetable flavour notes characteristic of conventional commercial pulse protein products and useful for the fortification of food and beverage products and prepared without the use of salt in the process. The pulse protein products of the present invention are obtained by extracting pulse protein source with water to form an aqueous pulse protein solution, at least partially separating the aqueous pulse protein solution from residual pulse protein source, adjusting the pH of the aqueous pulse protein solution to a pH of about 1.5 to about 3.4 to solubilize the bulk of the protein and form an acidified pulse protein solution then separating the acidified pulse protein solution from the acid insoluble solid material. The acidified pulse protein solution may be dried following optional concentration and diafiltration to form a pulse protein product, which may be an isolate. The acid insoluble solid material may be washed with acidified water and then dried to form another pulse protein product. These products may be dried at the acidic pH at which they were prepared or may be adjusted in pH before drying. Also described is the preparation of an acid soluble protein product, which may be an isolate, and which provides acidic solutions of improved clarity and is derived from the acidified pulse protein solution.

Preparation of pulse protein products (YP810)

The present invention is directed to non-soy oilseed protein products, very low in, or free of, beany, green, vegetable or similar flavour notes and useful for the fortification of food and beverage products and prepared without the use of salt in the process. The non-soy oilseed protein products of the present invention are obtained by extracting non-soy oilseed protein source with water to form an aqueous non-soy oilseed protein solution, at least partially separating the aqueous non-soy oilseed protein solution from residual non-soy oilseed protein source, adjusting the pH of the aqueous non-soy oilseed protein solution to a pH between about 1.5 and a value about 1 pH unit lower than the typical pH of isoelectric precipitation to solubilize the bulk of the protein and form an acidified non-soy oilseed protein solution then separating the acidified non-soy oilseed protein solution from the acid insoluble solid material. The acidified non-soy oilseed protein solution may be dried following optional concentration and diafiltration to form a non-soy oilseed protein product, which may be an isolate. The acid insoluble solid material may be washed with acidified water and then dried to form another non-soy oilseed protein product. These products may be dried at the acidic pH at which they were prepared or may be adjusted in pH before drying.

Preparation of non-soy oilseed protein products ('*810')

An aqueous solution of a pulse protein product having a protein content of at least about 60 wt % (N&#xd7;6.25) d.b. which is soluble in aqueous media at a pH of less than about 4.4 and heat stable at that pH range is adjusted in pH to a pH of about 6 to about 8. The resulting product is further processed by drying the product, recovering and drying any precipitated pulse protein material, heat treating and then drying the product, or heat treating the product and recovering and drying any precipitated pulse protein material.

pH adjusted pulse protein product

Canola protein products having a protein content of at least about 60 wt % (N&#xd7;6.25) d.b., preferably at least about 90 wt %, more preferably at lease about 100 wt %, and low phytic acid content, are produced by extracting canola seeds or canola oil seed meal with an aqueous calcium salt solution, preferably calcium chloride solution, to cause solubilization of canola protein from the seeds or meal.

Canola protein product with low phytic acid content ('C702')

Pulse proteins of reduced astringency are obtained by fractionating pulse protein products which are completely soluble and heat stable in aqueous media at acid pH value of less than about 4.4 into lower molecular weight, less astringent proteins and higher molecular weight, more astringent proteins.

Production of pulse protein product with reduced astringency

A soy protein product is obtained by extracting a soy protein source material with an aqueous calcium salt solution to form an aqueous soy protein solution and adjusting the pH of the mixture of aqueous soy protein solution and residual soy protein source to a pH of about 1.5 to about 4.4. The acidified soy protein solution then is separated from the residual soy protein source. The acidified soy protein solution may be dried, following optional concentration and diafiltration, to provide the soy protein product.

Production of soluble soy protein product ('S704')

A pulse protein product, which may be an isolate, produces heat-stable solutions at low pH values and is useful for the fortification of acidic beverages such as soft drinks and sports drinks without precipitation of protein. The pulse protein product is obtained by extracting a pulse protein source material with an aqueous calcium salt solution to form an aqueous pulse protein solution, separating the aqueous pulse protein solution from residual pulse protein source, adjusting the pH of the aqueous pulse protein solution to a pH of about 1.5 to about 4.4 to produce an acidified pulse protein solution, which may be dried, following optional concentration and diafiltration, to provide the pulse protein product.

Production of soluble protein solutions from pulses

The present invention is directed to soy protein products, very low in, or free of, beany flavor notes and useful for the fortification of food and beverage products and prepared without the use of salt in the process. The soy protein products of the present invention are obtained by extracting soy protein source with water to form an aqueous soy protein solution, at least partially separating the aqueous soy protein solution from residual soy protein source, adjusting the pH of the aqueous soy protein solution to a pH of about 1.5 to about 3.6 to solubilize at least a portion of the protein and form an acidified soy protein solution then separating the acidified soy protein solution from the acid insoluble solid material. The acidified soy protein solution may be dried following optional concentration and diafiltration to form a soy protein product, which may be an isolate. The acid insoluble solid material may be washed with acidified water and then dried to form another soy protein product. These products may be dried at the acidic pH at which they were prepared or may be adjusted in pH before drying.

Preparation of soy protein products ('S810')

pH-adjusted soy protein products, particularly isolates, that have a natural pH of about 6 and have a non-beany flavor are provided by the processing of soy protein product which is completely soluble in aqueous media at a pH of less than about 4.4 and heat stable in this pH range or a concentrated soy protein solution produced in the preparation of such soy protein product.

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Winnipeg, Canada

Kevin I Segall