| Patent application number | Description | Published |
|---|
| 20080299282 | Novel canola protein isolate - A novel canola protein isolate consisting predominantly of 2S canola protein and having equal to better solubility properties and improved clarity 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 or isoelectric precipitation 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. | 12-04-2008 |
| 20090036655 | Production of 2S Canola Protein Involving Ion Exchange - Substantially pure 2S canola protein is obtained substantially free from 7S and 12S canola protein by a procedure in which 2S canola protein is captured by binding to a cation-exchange medium while permitting other proteins and impurities to be washed away. The 2S canola protein then is removed from the cation-exchange medium by exposure of the cation-exchange medium to saline at a suitably high salt concentration. | 02-05-2009 |
| 20090203880 | Production of Canola Protein - A canola protein isolate having a protein content of at least about 90 wt % (N×6.25), preferably at least about 100 wt %, and consisting predominantly of the 2S protein and substantially free from the 7S and 12S proteins is prepared. In one aspect, canola oil seed meal is extracted with aqueous protein solution at an elevated temperature to preferentially extract 2S protein from the meal to produce a canola protein solution containing predominantly 2S protein. The 2S canola protein is recovered as an isolate. In another aspect, canola oil seed meal is initially extracted with water to preferentially extract 7S and 12S canola proteins followed by extraction of the canola oil seed meal with aqueous saline solution to extract 2S protein from the meal. 2S canola protein isolate is recovered from the saline extract. In another aspect, the canola oil seed meal is extracted with aqueous saline solution to extract 2S, 7S and 12S proteins from the meal. The aqueous protein extract solution is heat treated at an elevated temperature to precipitate 7S and 12S proteins and leave a 2S protein solution from which the isolate may be recovered. In a further aspect, the aqueous protein solution is concentrated prior to the heat treatment. | 08-13-2009 |
| 20090318671 | Novel canola protein isolate - A novel canola protein isolate consisting predominantly of 2S canola protein and having equal to better solubility properties and improved clarity 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 or isoelectric precipitation 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. | 12-24-2009 |
| 20100010198 | Soluble Canola Protein Isolate Production ("Nutratein") - Canola protein isolates are provided which contain both albumin and globulin protein fractions that are soluble and parent in an acidic aqueous environment. The canola protein isolates are completely soluble in water at low pH, low in phytic acid and useful in products for human consumption, pet foods and aquaculture. | 01-14-2010 |
| 20100034951 | Novel canola protein isolated - A novel canola protein isolate consisting predominantly of 2S canola protein and having equal to better solubility properties and improved clarity 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 or isoelectric precipitation 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. | 02-11-2010 |
| 20100036099 | Soluble canola protein isolate production ("nutratein") - Canola protein isolates are provided which contain both albumin and globulin protein fractions that are soluble, transparent and heat stable in an acidic aqueous environment. The canola protein isolates are completely soluble in water at low pH, low in phytic acid and useful in products for human consumption, pet foods and aquaculture. | 02-11-2010 |
| 20100040763 | Preparation of Canola Protein Isolate Without Heat Treatment ("C200Ca") - The supernatant from the deposition of canola protein micellar mass is processed to provide a canola protein isolate which is soluble in an aqueous acidic environment. | 02-18-2010 |
| 20100041871 | Preparation of Canola Protein Isolate from Canola Oil Seeds ("Blendertein") - Canola protein isolate is recovered from canola oil seeds by crushing the oil seeds and extracting the crushed canola oil seeds. Fat co-extracted from the crushed oil seeds is removed from the aqueous canola protein solution which then is processed by the micellar route to obtain the canola protein isolate. | 02-18-2010 |
| 20100048874 | Colour reduction in canola protein isolate - In the recovery of canola protein isolates from canola oil seeds steps are taken to inhibit the formation of colouring components and to reduce the presence of materials tending to form colouring components, to obtain a lighter and less yellow canola protein isolate. | 02-25-2010 |
| 20100048875 | Soluble Canola Protein Isolate Production from PMM ("C307") - A soluble canola protein isolate is prepared from canola protein micellar mass by solubilizing the protein micellar mass in a calcium salt solution, preferably a calcium chloride solution, followed by dilution of the resulting canola protein solution. Following removal of the precipitate phytic acid, the aqueous canola protein solution is concentrated, optionally diafiltered, and acidified to a pH of about 2.5 to 4.0 to produce an acidified clear canola protein solution, which may be concentrated, subjected to a colour removal step and dried. The canola protein isolate so formed is soluble, transparent and heat stable in an acid aqueous environment and also is soluble at natural pH, without precipitation of protein. | 02-25-2010 |
| 20100068370 | Emulsified Foods - Emulsified foods are provided in which whole egg or egg yolk, conventionally employed to formulate such foods, such as mayonnaises, is replaced, in whole or in part, by a canola protein isolate, which may be a PMM-derived canola protein isolate, the canola protein isolate directly obtained from the supernatant from the formation of PMM or the canola protein isolate obtained following heat treatment. | 03-18-2010 |
| 20100098818 | Production of Soluble Protein Solutions from Soy ("S701") - A soy protein product, which may be an isolate, produces transparent heat-stable solutions at low pH values and is useful for the fortification of soft drinks and sports drinks without precipitation of protein. The 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, 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 4.4 to produce an acidified clear soy protein solution, which may be dried, following optional concentration and diafiltration, to provide the soy protein product. | 04-22-2010 |
| 20100173064 | Novel canola protein isolate - A novel canola protein isolate consisting predominantly of 2S canola protein and having equal to better solubility properties and improved clarity properties in aqueous media, has an increased proportion of 2S canola protein and a decreased proportion of 7S canola protein. The novel canola protein isolate is formed by isoelectric precipitation of aqueous supernatant from canola protein micelle formation and precipitation, to effect precipitation of 7S protein which is sedimented and removed. | 07-08-2010 |
| 20100179305 | Protein isolation procedures for reducing phytic acid - Oil seed protein isolates, in particular canola protein isolate, having a decreased phytic acid content is prepared by a procedure in which extraction of phytic acid from oil seed meal is inhibited during extraction of protein from the oil seed meal. | 07-15-2010 |
| 20100184956 | PRODUCTION OF 2S CANOLA PROTEIN INVOLVING ION EXCHANGE - Substantially pure 2S canola protein is obtained substantially free from 7S and 12S canola protein by a procedure in which 2S canola protein is captured by binding to a cation-exchange medium while permitting other proteins and impurities to be washed away. The 2S canola protein then is removed from the cation-exchange medium by exposure of the cation-exchange medium to saline at a suitably high salt concentration. | 07-22-2010 |
| 20100189852 | Production of Soluble Soy Protein Product from Soy Protein Micellar Mass ("S500") - A soy protein product having a protein content of at least 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed by extracting soy protein source material to solubilize soy protein in the source material and to form an aqueous soy protein solution having a pH of about 5 to about 7, concentrating the aqueous soy protein solution to a concentration of about 50 to about 400 g/L to form a concentrated soy protein isolate, optionally diafiltering the concentrated soy protein solution, and drying the soy protein solution. The soy protein product is soluble in acidic media and produces transparent, heat stable solutions at low pH values and, therefore, may be used for protein fortification of soft drinks and sports drinks. | 07-29-2010 |
| 20100189853 | Production of Soluble Soy Protein Product from Soy Protein Micellar Mass ("S200Ca") - A soy protein product having a protein content of at least 60 wt % (N×6.25) d.b., preferably an isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed from the supernatant from the precipitation of a soy protein micellar mass. A calcium salt or other divalent salt is added to the supernatant, before concentration, after initial concentration or after final concentration, to provide a conductivity of about 2 to about 30 mS. Precipitate is removed from the resulting solution and the pH of the clear soy protein solution is optionally adjusted to about 1.5 to about 4.4. The optionally pH-adjusted clear solution is concentrated to a concentration of about 50 to about 400 g/L and the clear concentrated protein solution is optionally diafiltered prior to drying. The soy protein product is soluble in acidic media and produces transparent, heat stable solutions at low pH values and, therefore, may be used for protein fortification of soft drinks and sports drinks. | 07-29-2010 |
| 20100203203 | Preparation of Soy Protein Product Using Water Extraction ("S803") - A soy protein product which is completely soluble and is capable of providing transparent and heat stable solutions at low and neutral pH values is produced by extracting a soy protein source material with water at low pH, subjecting the resulting aqueous soy protein solution to ultrafiltration and optional diafiltration to provide a concentrated and optionally diafiltered soy protein solution, which may be dried to provide the soy protein product. The soy protein product may be used for protein fortification of, in particular, soft drinks and sports drinks, without precipitation of protein. | 08-12-2010 |
| 20100203204 | Production of Soy Protein Product Using Calcium Chloride Extraction ("S7300/S7200") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 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, preferably calcium chloride 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, diluting the concentrated and optionally diafiltered with water to cause the formation of a precipitate, separating the precipitate from the diluting water (supernatant), and drying the separated soy protein solution to provide the soy protein product. The supernatant may be processed to form soy protein products having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 wt % (N×6.25) d.b. | 08-12-2010 |
| 20100203205 | Production of Soy Protein Product Using Calcium Chloride Extraction ("S702") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 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, preferably calcium chloride 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. | 08-12-2010 |
| 20100215830 | Production of Soy Protein Product Using Calcium Chloride Extraction ("S7301") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 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, preferably calcium chloride 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, diluting the concentrated and optionally diafiltered soy protein solution into water to cause the formation of a precipitate, acidifying the mixture of precipitate and diluting water to re-solubilize the precipitate and form a clear acidified soy protein solution, concentrating the clear acidified soy protein solution while maintaining the ionic strength substantially constant by using a selective membrane technique, optionally diafiltering the concentrated clear acidified soy protein solution, and drying the concentrated and optionally diafiltered clear acidified soy protein solution. | 08-26-2010 |
| 20100221403 | Production of Soluble Soy Protein Product from Soy Protein Micellar Mass ("S300/S200") - A soy protein product having a protein content of at least 60 wt % (N×6.25) dry weight, preferably a soy protein isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed by a soy protein micellar mass production route. The supernatant from the coalesced protein micellar mass may be processed to recover additional quantities of soy protein product. The soy protein product may be used for a fortification of soft drinks and sports drinks. | 09-02-2010 |
| 20100291285 | Production of canola protein product without heat treatment ("C200CaC") - The supernatant from the deposition of canola protein micellar mass is processed to provide a canola protein product having a protein content of about 60 to less than about 90 wt % (N×6.25) protein on a dry weight basis and which is soluble in an aqueous acidic environment. | 11-18-2010 |
| 20100330248 | Production of Acid Soluble Soy Protein Isolates ("S700") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably an isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed by extracting a soy protein source with a salt solution, preferably aqueous sodium chloride solution, to form an aqueous protein solution having a pH of about 1.5 to 11, preferably about 5 to about 7 and separating the resulting aqueous protein solution from residual soy protein source. The protein concentration of the aqueous protein solution is increased to about 50 to about 400 g/L while the ionic strength is maintained substantially constant by using a selective membrane technique. The resulting concentrated protein solution is optionally diafiltered and a calcium salt, preferably calcium chloride, is added to the concentrated and optionally diafiltered protein solution to a conductivity of 15 to about 85 mS. Precipitate formed as a result of the calcium salt addition is removed and the resulting clarified retentate is diluted into about 2 to about 20 volumes of water prior to acidification to a pH of about 1.5 to about 4.4 to produce an acidified clear protein solution. The acidified clear protein solution is then concentrated and optionally diafiltered and optionally dried. Variations of this procedure can be used to produce a soy protein product which is soluble, transparent and heat stable in acidic aqueous environments. | 12-30-2010 |
| 20100330249 | Preparation of Soy Protein Isolate Using Calcium Chloride Extraction ("S703") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably an isolate, is formed by a procedure in which soy protein is extracted from a soy source material using an aqueous calcium chloride solution at low pH, generally about 1.5 to about 5, and separating the resulting aqueous soy protein solution from residual soy protein source. The resulting clarified aqueous soy protein solution may be diluted and the pH adjusted within the range of 1.5-5.0. The solution may be concentrated by ultrafiltration, diafiltered and then dried to provide the soy protein product. The soy protein product is soluble in acidic medium and produces transparent, heat stable solutions and hence may be used for protein fortification of soft drinks and sports drinks. | 12-30-2010 |
| 20100330250 | Production of Acid Soluble Soy Protein Isolates ("S800") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably an isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed by extracting a soy protein source with water to form an aqueous protein solution having a pH of about 1.5 to about 11, preferably about 5 to about 7, and separating the resulting aqueous protein solution from residual soy protein source. The protein concentration of the aqueous protein solution is increased to about 50 to about 400 g/L while the ionic strength is maintained substantially constant by using a selective membrane technique. The resulting concentrated protein solution is optionally diafiltered and a calcium salt, preferably calcium chloride, is added to the concentrated and optionally diafiltered protein solution to a conductivity of 5 to about 30 mS. Precipitate formed as a result of the calcium salt addition is removed and the resulting clarified retentate is diluted into about 2 to about 20 volumes of water prior to acidification to a pH of about 1.5 to about 4.4 to produce an acidified clear protein solution. The acidified clear protein solution is then concentrated and optionally diafiltered and optionally dried. Variations of this procedure can be used to produce a soy protein product which is soluble, transparent and heat stable in acidic aqueous environments. | 12-30-2010 |
| 20110038993 | Production of soluble protein solutions from soy ("S701" CIP) - A soy protein product, which may be an isolate, produces transparent heat-stable solutions at low pH values and is useful for the fortification of soft drinks and sports drinks without precipitation of protein. The 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, 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 4.4 to produce an acidified clear soy protein solution, which may be dried, following optional concentration and diafiltration, to provide the soy protein product. | 02-17-2011 |
| 20110070343 | Canola protein product from supernatant - A novel canola protein product 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, and a protein content of less than about 90 wt % (N×6.25) d.b. The novel canola protein isolate is formed by heat treatment or isoelectric precipitation of aqueous supernatant from canola protein micelle formation and precipitation, to effect precipitation of 7S protein which is sedimented and removed. | 03-24-2011 |
| 20110159166 | Novel canola protein isolate - 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. | 06-30-2011 |
| 20110165314 | pH Adjusted Soy Protein Isolate and Uses - pH-adjusted soy protein products, particularly isolates, that have a natural pH of about 6 and have a non-beany flavour 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. | 07-07-2011 |
| 20110172395 | SOLUBLE CANOLA PROTEIN ISOLATE PRODUCTION - Canola protein isolates are provided which contain both albumin and globulin protein fractions that are soluble and transparent in an acidic aqueous environment. The canola protein isolates are completely soluble in water at low pH, low in phytic acid and useful in products for human consumption, pet foods and aquaculture. | 07-14-2011 |
| 20110172396 | SOLUBLE CANOLA PROTEIN ISOLATE PRODUCTION FROM PROTEIN MICELLAR MASS - A soluble canola protein isolate is prepared from canola protein micellar mass by solubilizing the protein micellar mass in a calcium salt solution, preferably a calcium chloride solution, followed by dilution of the resulting canola protein solution. Following removal of the precipitate phytic acid, the aqueous canola protein solution is concentrated, optionally diafiltered, and acidified to a pH of about 2.5 to 4.0 to produce an acidified clear canola protein solution, which may be concentrated, subjected to a colour removal step and dried. The canola protein isolate so formed is soluble, transparent and heat stable in an acid aqueous environment and also is soluble at natural pH, without precipitation of protein. | 07-14-2011 |
| 20110184149 | PREPARATION OF CANOLA PROTEIN ISOLATE FROM CANOLA OIL SEEDS ("BLENDERTEIN") - Canola protein isolate is recovered from canola oil seeds by crushing the oil seeds and extracting the crushed canola oil seeds. Fat co-extracted from the crushed oil seeds is removed from the aqueous canola protein solution which then is processed by the micellar route to obtain the canola protein isolate. | 07-28-2011 |
| 20110189371 | PRODUCTION OF CANOLA PROTEIN ISOLATE WITHOUT HEAT TREATMENT - The supernatant from the deposition of canola protein micellar mass is processed to provide a canola protein isolate which is soluble in an aqueous acidic environment. | 08-04-2011 |
| 20110200720 | NOVEL CANOLA PROTEIN ISOLATE - A novel canola protein isolate consisting process predominantly of 2S canola protein and having equal to better solubility properties and improved clarity properties in aqueous media, has an increased proportion of 2S canola protein and a decreased proportion of 7S canola protein. The novel canola protein isolate is formed by isoelectric precipitation of aqueous supernatant from canola protein micelle formation and precipitation, to effect precipitation isoelectric precipitation isoelectric precipitation of 7S protein which is sedimented and removed. | 08-18-2011 |
| 20110206825 | EMULSIFIED FOODS - Emulsified foods are provided in which whole egg or egg yolk, conventionally employed to formulate such foods, such as mayonnaises, is replaced, in whole or in part, by a canola protein isolate, which may be a PMM-derived canola protein isolate, the canola protein isolate directly obtained from the supernatant from the formation of PMM or the canola protein isolate obtained following heat treatment. | 08-25-2011 |
| 20110223295 | Preparation of soy protein isolate using calcium chloride extraction ("S703 CIP") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably an isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed by a procedure in which soy protein is extracted from a soy source material using an aqueous calcium chloride solution at low pH, generally about 1.5 to about 5, and separating the resulting aqueous soy protein solution from residual soy protein source. The resulting clarified aqueous soy protein solution may be diluted and the pH adjusted within the range of 1.5-5.0. The solution may be concentrated by ultrafiltration, diafiltered and then dried to provide the soy protein product. Alternatively, the concentrated and optionally diafiltered soy protein solution may be optionally adjusted in pH within the range of 1.5-7.0 then diluted into water to cause the formation of a precipitate, separating the precipitate from the diluting water (supernatant) and drying the separated soy protein to form a soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 wt % (N×6.25) d.b. The supernatant may be processed to form soy protein products having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least 90 wt % (N×6.25) d.b. Alternatively, the precipitate from the dilution step may be re-solubilized in the diluting water by adjustment of the pH to resolubilize the precipitate and form a protein solution. The soy protein solution may be concentrated while maintaining the ionic strength substantially constant by using a selective membrane technique followed by optional diafiltration and drying. The soy protein product is soluble in acidic medium and produces transparent, heat stable solutions and hence may be used for protein fortification of soft drinks and sports drinks. | 09-15-2011 |
| 20110236556 | PRODUCTION OF SOLUBLE PROTEIN SOLUTIONS FROM SOY ("S701") - A soy protein product, which may be an isolate, produces transparent heat-stable solutions at low pH values and is useful for the fortification of soft drinks and sports drinks without precipitation of protein. The 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, 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 4.4 to produce an acidified clear soy protein solution, which may be dried, following optional concentration and diafiltration, to provide the soy protein product. | 09-29-2011 |
| 20110274797 | PRODUCTION OF SOLUBLE PROTEIN SOLUTIONS FROM PULSES - A pulse protein product, which may be an isolate, produces heat-stable solutions at low pH values and is useful for the fortification of 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. | 11-10-2011 |
| 20120027911 | PREPARATION OF SOY PROTEIN PRODUCT USING WATER EXTRACTION ("S803") - A soy protein product which is completely soluble and is capable of providing transparent and heat stable solutions at low and neutral pH values is produced by extracting a soy protein source material with water at low pH, subjecting the resulting aqueous soy protein solution to ultrafiltration and optional diafiltration to provide a concentrated and optionally diafiltered soy protein solution, which may be dried to provide the soy protein product. The soy protein product may be used for protein fortification of in particular, soft drinks and sports drinks, without precipitation of protein. | 02-02-2012 |
| 20120040074 | PRODUCTION OF SOY PROTEIN PRODUCT USING CALCIUM CHLORIDE EXTRACTION "(S702/S7300/S7200/S7301") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 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, preferably calcium chloride 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. Alternatively, the concentrated and optionally diafiltered soy protein solution may be diluted into water to cause the formation of a precipitate, separating the precipitate from the diluting water (supernatant), and drying the separated soy protein solution to form a soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 wt % (N×6.25) d.b. The supernatant may be processed to form soy protein products having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least 90 wt % (N×6.25) d.b. Alternatively, the precipitate from the dilution step and diluting water is acidified to resolubilize the precipitate and form a clear soy protein solution. The clear soy protein solution is concentrated while maintaining the ionic strength substantially constant by using a selective membrane technique followed by optional diafiltration and drying. | 02-16-2012 |
| 20120107484 | PRODUCTION OF CANOLA PROTEIN PRODUCT WITHOUT HEAT TREATMENT ("C200CaC") - The supernatant from the deposition of canola protein micellar mass is processed to provide a canola protein product having a protein content of about 60 to less than about 90 wt % (N×6.25) protein on a dry weight basis and which is soluble in an aqueous acidic environment. | 05-03-2012 |
| 20120116055 | NOVEL CANOLA PROTEIN ISOLATE - 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. | 05-10-2012 |
| 20120130051 | ASTRINGENCY IN SOY PROTEIN SOLUTIONS - A soy protein product having reduced astringency, which may be an isolate, produces transparent heat-stable solutions at low pH values and is useful for the fortification of soft drinks and sports drinks without precipitation of protein. The 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, 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 4.4 using at least one organic acid, such as citric acid or a blend of citric acid and malic acid or a mixture of at least one organic acid and at least one mineral acid, such as hydrochloric acid and phosphoric acid, to produce an acidified clear soy protein solution, which may be dried directly or following optional concentration and diafiltration, to provide the soy protein product. | 05-24-2012 |
| 20120135117 | PRODUCTION OF SOLUBLE PROTEIN SOLUTIONS FROM PULSES - 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. | 05-31-2012 |
| 20120141651 | PREPARATION OF SOY PROTEIN ISOLATE USING CALCIUM CHLORIDE EXTRACTION ("S703") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably an isolate, is formed by a procedure in which soy protein is extracted from a soy source material using an aqueous calcium chloride solution at low pH, generally about 1.5 to about 5, and separating the resulting aqueous soy protein solution from residual soy protein source. The resulting clarified aqueous soy protein solution may be diluted and the pH adjusted within the range of 1.5-5.0. The solution may be concentrated by ultrafiltration, diafiltered and then dried to provide the soy protein product. The soy protein product is soluble in acidic medium and produces transparent, heat stable solutions and hence may be used for protein fortification of soft drinks and sports drinks. | 06-07-2012 |
| 20120157661 | SOY PROTEIN PRODUCTS OF IMPROVED WATER-BINDING CAPACITY - Soy protein products are provided which lack the characteristic beany flavour of conventional soy protein isolates and can replace conventional isolates in various food products to provide food products having improved flavour. | 06-21-2012 |
| 20120164301 | PRODUCTION OF ACID SOLUBLE SOY PROTEIN ISOLATES ("S700") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably an isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed by extracting a soy protein source with a salt solution, preferably aqueous sodium chloride solution, to form an aqueous protein solution having a pH of about 1.5 to 11, preferably about 5 to about 7 and separating the resulting aqueous protein solution from residual soy protein source. The protein concentration of the aqueous protein solution is increased to about 50 to about 400 g/L while the ionic strength is maintained substantially constant by using a selective membrane technique. The resulting concentrated protein solution is optionally diafiltered and a calcium salt, preferably calcium chloride, is added to the concentrated and optionally diafiltered protein solution to a conductivity of 15 to about 85 mS. Precipitate formed as a result of the calcium salt addition is removed and the resulting clarified retentate is diluted into about 2 to about 20 volumes of water prior to acidification to a pH of about 1.5 to about 4.4 to produce an acidified clear protein solution. The acidified clear protein solution is then concentrated and optionally diafiltered and optionally dried. Variations of this procedure can be used to produce a soy protein product which is soluble, transparent and heat stable in acidic aqueous environments. | 06-28-2012 |
| 20120171348 | PRODUCTION OF ACID SOLUBLE SOY PROTEIN ISOLATES ("S800") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably an isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is formed by extracting a soy protein source with water to form an aqueous protein solution having a pH of about 1.5 to about 11, preferably about 5 to about 7, and separating the resulting aqueous protein solution from residual soy protein source. The protein concentration of the aqueous protein solution is increased to about 50 to about 400 g/L while the ionic strength is maintained substantially constant by using a selective membrane technique. The resulting concentrated protein solution is optionally diafiltered and a calcium salt, preferably calcium chloride, is added to the concentrated and optionally diafiltered protein solution to a conductivity of 5 to about 30 mS. Precipitate formed as a result of the calcium salt addition is removed and the resulting clarified retentate is diluted into about 2 to about 20 volumes of water prior to acidification to a pH of about 1.5 to about 4.4 to produce an acidified clear protein solution. The acidified clear protein solution is then concentrated and optionally diafiltered and optionally dried. Variations of this procedure can be used to produce a soy protein product which is soluble, transparent and heat stable in acidic aqueous environments. | 07-05-2012 |
| 20120269948 | CANOLA PROTEIN PRODUCT FROM SUPERNATANT - A novel canola protein product consisting predominantly of 2S canola protein and having improved solubility properties, has an increased proportion of 2 S canola protein and a decreased proportion of 7S canola protein, and a protein content of less than about 90 wt % (N×6.25) d.b. The novel canola protein isolate is formed by heat treatment or isoelectric precipitation of aqueous supernatant from canola protein micelle formation and precipitation, to effect precipitation of 7S protein which is sedimented and removed. | 10-25-2012 |
| 20120295008 | PRODUCTION OF SOLUBLE SOY PROTEIN PRODUCT ("S704") - 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. | 11-22-2012 |
| 20120322980 | pH ADJUSTED SOY PROTEIN ISOLATE AND USES - pH-adjusted soy protein products, particularly isolates, that have a natural pH of about 6 and have a non-beany flavour 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. | 12-20-2012 |
| 20130005946 | CANOLA PROTEIN PRODUCT WITH LOW PHYTIC ACID CONTENT ("C702") - Canola protein products having a protein content of at least about 60 wt % (N×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. | 01-03-2013 |
| 20130078355 | PRODUCTION OF SOLUBLE PROTEIN SOLUTIONS FROM SOY ("S701" CIP) - A soy protein product, which may be an isolate, produces transparent heat-stable solutions at low pH values and is useful for the fortification of soft drinks and sports drinks without precipitation of protein. The 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, 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 4.4 to produce an acidified clear soy protein solution, which may be dried, following optional concentration and diafiltration, to provide the soy protein product. | 03-28-2013 |
| 20130101713 | PRODUCTION OF SOY PROTEIN PRODUCT USING CALCIUM CHLORIDE EXTRACTION ("S702") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 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, preferably calcium chloride 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. | 04-25-2013 |
| 20130129901 | PRODUCTION OF SOLUBLE PROTEIN SOLUTIONS FROM PULSES - A pulse protein product, which may be an isolate, produces heat-stable solutions at low pH values and is useful for the fortification of 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. | 05-23-2013 |
| 20130131316 | PREPARATION OF CANOLA PROTEIN ISOLATE FROM CANOLA OIL SEEDS ("BLENDERTEIN") - Canola protein isolate is recovered from canola oil seeds by crushing the oil seeds and extracting the crushed canola oil seeds. Fat co-extracted from the crushed oil seeds is removed from the aqueous canola protein solution which then is processed by the micellar route to obtain the canola protein isolate. | 05-23-2013 |
| 20130189408 | PRODUCTION OF SOLUBLE PROTEIN SOLUTIONS FROM PULSES - 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. | 07-25-2013 |
| 20130209654 | FROZEN DESSERT MIXES USING CANOLA PROTEIN PRODUCTS - A canola protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably at least about 90 wt %, and consisting predominantly of 2S canola protein and derived from supernatant from a protein micellar mass settling step is used to provide, at least in part, the protein component of a dairy analogue or plant/dairy blend frozen dessert mix. | 08-15-2013 |
| 20130216684 | NOVEL CANOLA PROTEIN ISOLATE - A novel canola protein isolate consisting predominantly of 2S canola protein and having equal to better solubility properties and improved clarity 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 or isoelectric precipitation 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. | 08-22-2013 |
| 20130236628 | FROZEN DESSERT MIXES USING SOY PROTEIN PRODUCTS - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably at least about 90 wt %, and being completely soluble at pH values of less than about 4.4 and heat stable at such pH values is used to provide, at least in part, the protein component of a dairy analogue or plant/dairy blend frozen dessert mix. | 09-12-2013 |
| 20130253171 | COLOUR REDUCTION IN CANOLA PROTEIN ISOLATE - In the recovery of canola protein isolates from canola oil seeds steps are taken to inhibit the formation of colouring components and to reduce the presence of materials tending to form colouring components, to obtain a lighter and less yellow canola protein isolate. | 09-26-2013 |
| 20130281670 | SOLUBLE CANOLA PROTEIN ISOLATE PRODUCTION ("NUTRATEIN") - Canola protein isolates are provided which contain both albumin and globulin protein fractions that are soluble, transparent and heat stable in an acidic aqueous environment. The canola protein isolates are completely soluble in water at low pH, low in phytic acid and useful in products for human consumption, pet foods and aquaculture. | 10-24-2013 |
| 20130287928 | PRODUCTION OF SOLUBLE PROTEIN PRODUCTS FROM PULSES - Protein products from pulses are obtained using procedures in which calcium chloride is used in multiple extractions of pulse protein source material. | 10-31-2013 |
| 20130287929 | PRODUCTION OF SOLUBLE PROTEIN PRODUCTS FROM PULSES - Protein products from pulses are obtained using procedures in which calcium chloride is used in multiple extractions of pulse protein source material. | 10-31-2013 |
| 20130303730 | ASTRINGENCY IN SOY PROTEIN SOLUTIONS - A soy protein product having reduced astringency, which may be an isolate, produces transparent heat-stable solutions at low pH values and is useful for the fortification of soft drinks and sports drinks without precipitation of protein. The 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, 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 4.4 using at least one organic acid, such as citric acid or a blend of citric acid and malic acid or a mixture of at least one organic acid and at least one mineral acid, such as hydrochloric acid and phosphoric acid, to produce an acidified clear soy protein solution, which may be dried directly or following optional concentration and diafiltration, to provide the soy protein product. | 11-14-2013 |
| 20130316069 | PRODUCTION OF SOLUBLE PROTEIN SOLUTIONS FROM SOY ("S701" CIP) - A soy protein product, which may be an isolate, produces transparent heat-stable solutions at low pH values and is useful for the fortification of soft drinks and sports drinks without precipitation of protein. The 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, 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 4.4 to produce an acidified clear soy protein solution, which may be dried, following optional concentration and diafiltration, to provide the soy protein product. | 11-28-2013 |
| 20130331551 | PREPARATION OF CANOLA PROTEIN ISOLATE FROM CANOLA OIL SEEDS ("BLENDERTEIN") - Canola protein isolate is recovered from canola oil seeds by crushing the oil seeds and extracting the crushed canola oil seeds. Fat co-extracted from the crushed oil seeds is removed from the aqueous canola protein solution which then is processed by the micellar route to obtain the canola protein isolate. | 12-12-2013 |
| 20140004246 | PRODUCTION OF SOLUBLE PROTEIN PRODUCTS FROM PULSES | 01-02-2014 |
| 20140017379 | PH ADJUSTED PULSE PROTEIN PRODUCT - An aqueous solution of a pulse protein product having a protein content of at least about 60 wt % (N×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. | 01-16-2014 |
| 20140017387 | EMULSIFIED FOODS - Emulsified foods are provided in which whole egg or egg yolk, conventionally employed to formulate such foods, such as mayonnaises, is replaced, in whole or in part, by a canola protein isolate, which may be a PMM-derived canola protein isolate, the canola protein isolate directly obtained from the supernatant from the formation of PMM or the canola protein isolate obtained following heat treatment. | 01-16-2014 |
| 20140065289 | PH ADJUSTED SOY PROTEIN ISOLATE AND USES - pH-adjusted soy protein products, particularly isolates, that have a natural pH of about 6 and have a non-beany flavour 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. | 03-06-2014 |
| 20140093626 | PRODUCTION OF PULSE PROTEIN PRODUCT USING CALCIUM CHLORIDE EXTRACTION ("YP702") - A pulse protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a pulse protein isolate having a protein content of at least about 90 wt % (N×6.25) d.b., is prepared from a pulse protein source material by extraction of the pulse protein source material with an aqueous calcium salt solution, preferably calcium chloride solution, to cause solubilization of pulse protein from the protein source and to form an aqueous pulse protein solution, separating the aqueous pulse protein solution from residual pulse protein source, optionally concentrating the aqueous pulse protein solution while maintaining the ionic strength substantially constant by using a selective membrane technique, optionally diafiltering the optionally concentrated pulse protein solution, and optionally drying the optionally concentrated and optionally diafiltered pulse protein solution. | 04-03-2014 |
| 20140106056 | PRODUCTION OF SOLUBLE SOY PROTEIN PRODUCT ("S704") - 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. | 04-17-2014 |
| 20140161956 | PRODUCTION OF SOY PROTEIN PRODUCT USING CALCIUM CHLORIDE EXTRACTION ("S702") - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably a soy protein isolate having a protein content of at least about 90 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, preferably calcium chloride 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. | 06-12-2014 |
| 20140221617 | CANOLA PROTEIN PRODUCT WITH LOW PHYTIC ACID CONTENT ("C702") - Canola protein products having a protein content of at least about 60 wt % (N×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. | 08-07-2014 |
| 20140255591 | FROZEN DESSERT MIXES USING SOY PROTEIN PRODUCTS - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably at least about 90 wt %, and being completely soluble at pH values of less than about 4.4 and heat stable at such pH values is used to provide, at least in part, the protein component of a dairy analogue or plant/dairy blend frozen dessert mix. | 09-11-2014 |
| 20140356510 | PRODUCTION OF PULSE PROTEIN PRODUCTS WITH REDUCED ASTRINGENCY - 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. | 12-04-2014 |
| 20150037490 | FROZEN DESSERT MIXES USING CANOLA PROTEIN PRODUCTS - A canola protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably at least about 90 wt %, and consisting predominantly of 2S canola protein and derived from supernatant from a protein micellar mass settling step is used to provide, at least in part, the protein component of a dairy analogue or plant/dairy blend frozen dessert mix. | 02-05-2015 |
| 20150079263 | FROZEN DESSERT MIXES USING SOY PROTEIN PRODUCTS - A soy protein product having a protein content of at least about 60 wt % (N×6.25) d.b., preferably at least about 90 wt %, and being completely soluble at pH values of less than about 4.4 and heat stable at such pH values is used to provide, at least in part, the protein component of a dairy analogue or plant/dairy blend frozen dessert mix. | 03-19-2015 |
