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US3911159A Expired / Lapsed US ⏱️ 0.0 years remaining

Protein fiber forming

Assignee: Nestle Purina PetCare Co
•
Filing: 1973-11-05
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Granted: 1975-10-07
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Expires: 1993-11-05
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Abstract

Abstract A process of continuously forming filamentous protein structures of improved tenderness is disclosed. The structures are formed from an aqueous slurry of a proteinaceous material and material, selected from the group consisting of cellulose and carbohydrate by-products from the processing of protein containing vegetable materials and grains said slurry having a solids content of at least about 20% by weight. The slurry should contain protein in an amount of at least about 40 percent by weight on a dry basis. The proteinaceous slurry is then formed into textured filamentous protein structures or fibers by continuously heating the slurry under pressure and cooling the slurry. The texture of the protein structures can be readily controlled by the process conditions, starting material, or reagents used in the process.

Inventors

  • 👤 Wilhelmus Heusdens

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 13:26
CPC Classifications
A; A23; A23J; A23J3/00; A23J3/22; A23J3/26; A23J3/265; Y; Y10; Y10S; Y10S426/00; Y10S426/802

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 219 words
A METHOD OF CONTINUOUSLY FORMING DISCRETE ELONGATED TENDER PROTEIN FILAMENTS FROM PROTEINACEOUS MATERIAL COMPRISING: A. FORMING A PUMPABLE SLURRY OF A MIXTURE OF A PROTEIN CONTAINING MATERIAL AND AN ADDED MATERIAL SELECTED FROM THE GROUP CONSISTING OF CELLULOSE AND CARBOHYDRATE BYPRODUCTS FROM THE PROCESSING OF PROTEIN CONTAINING VEGETABLE MATERIALS AND GRAINS, THE SLURRY HAVING A SOLIDS CONTENT OF ABOVE ABOUT 20% BY WEIGHT AND A PROTEIN CONTENT OF ABOVE ABOUT 40% BY WEIGHT ON A DRY BASIS, B. HYDRATING THE PROTEINACEOUS MATERIAL IN THE SLURRY TO PLACE THE PROTEINACEOUS MATERIAL IN A SUFFICIENTLY REACTIVE FORM TO PRODUCE ELONGATED PROTEIN FILAMENTS C. FORMING DISCRETE ELONGATED PROTEIN FILAMENTS BY CONTINUOUSLY CONDUCTING THE PROTEINACEOUS SLURRY UNDER PRESSURE THROUGH A HEAT EXCHANGE ZONE AND HEATING THE SLURRY TO A TEMPERATURE WHICH IS LESS THAN THAT WHICH WILL DEGRADE THE PROTEIN, WHILE THE PROTEIN IS SUBJECTED TO SUCH TEMPERATURE FOR A SUFFICIENT PERIOD OF TIME SO THAT ELONGATED TENDER FILAMENTS ARE SEPARATED FORM THE REMAINING CONSITUENTS OF THE SLURRY, CONTINUOUSLY REMOVING THE HEATED SLURRY FOM SAID ZONE THROUGH A BACK PRESSURE CREATING ORIFICE AND DISCHARGING THE FORMED DISCRETE ELONGATED FILAMENTS AND REMAINING CONSTITUENTS OF THE SLURRY INTO A COLLECTING ZONE, AND D. IN SAID COLLECTING ZONE SEPARATING THE TENDER ELONGATED PROTEIN FILAMENTS FROM THE REMAINING CONSTITUENTS OF THE SLURRY AND RECOVERING SAID DISCRETE FILAMENTS.
Claim 2
Independent Claim 219 words
A METHOD OF CONTINUOUSLY FORMING DISCRETE ELONGATED TENDER PROTEIN FILAMENTS FROM PROTEINACEOUS MATERIAL COMPRISING: A. FORMING A PUMPABLE SLURRY OF A MIXTURE OF A PROTEIN CONTAINING MATERIAL AND AN ADDED MATERIAL SELECTED FROM THE GROUP CONSISTING OF CELLULOSE AND CARBOHYDRATE BYPRODUCTS FROM THE PROCESSING OF PROTEIN CONTAINING VEGETABLE MATERIALS AND GRAINS, THE SLURRY HAVING A SOLIDS CONTENT OF ABOVE ABOUT 20% BY WEIGHT AND A PROTEIN CONTENT OF ABOVE ABOUT 40% BY WEIGHT ON A DRY BASIS, B. HYDRATING THE PROTEINACEOUS MATERIAL IN THE SLURRY TO PLACE THE PROTEINACEOUS MATERIAL IN A SUFFICIENTLY REACTIVE FORM TO PRODUCE ELONGATED PROTEIN FILAMENTS C. FORMING DISCRETE ELONGATED PROTEIN FILAMENTS BY CONTINUOUSLY CONDUCTING THE PROTEINACEOUS SLURRY UNDER PRESSURE THROUGH A HEAT EXCHANGE ZONE AND HEATING THE SLURRY TO A TEMPERATURE WHICH IS LESS THAN THAT WHICH WILL DEGRADE THE PROTEIN, WHILE THE PROTEIN IS SUBJECTED TO SUCH TEMPERATURE FOR A SUFFICIENT PERIOD OF TIME SO THAT ELONGATED TENDER FILAMENTS ARE SEPARATED FORM THE REMAINING CONSITUENTS OF THE SLURRY, CONTINUOUSLY REMOVING THE HEATED SLURRY FOM SAID ZONE THROUGH A BACK PRESSURE CREATING ORIFICE AND DISCHARGING THE FORMED DISCRETE ELONGATED FILAMENTS AND REMAINING CONSTITUENTS OF THE SLURRY INTO A COLLECTING ZONE, AND D. IN SAID COLLECTING ZONE SEPARATING THE TENDER ELONGATED PROTEIN FILAMENTS FROM THE REMAINING CONSTITUENTS OF THE SLURRY AND RECOVERING SAID DISCRETE FILAMENTS.
Claim 3
Dependent Claim 22 words
The method of claim 1 wherein the slurry is heated in the heat exchange zone to a temperature of above about 240*F.
Claim 4
Dependent Claim 20 words
The method of claim 1 wherein the slurry is heated with an injection heat exchanger in the heat exchange zone.
Claim 5
Dependent Claim 23 words
The method of claim 1 wherein the slurry is heated in the heat exchange zone to a temperature between about 240* - 315*F.
Claim 6
Dependent Claim 26 words
The method of claim 1 wherein the pressure to which the slurry is subjected in the heat exchange zone is between about 50 and 5,000 psig.
Claim 7
Dependent Claim 11 words
The method of claim 1 wherein the added material is cellulose.
Claim 8
Dependent Claim 22 words
The method of claim 1 wherein the protein containing material is selected from the group consisting of soy protein, albumen and casein.
Claim 9
Dependent Claim 30 words
A method of claim 1 wherein a chemical agent selected from the group consisting of phosphoric acid salts and citric acid salts is added to the slurry prior to heating.
Claim 10
Dependent Claim 19 words
The method of claim 1 wherein the step of hydrating the proteinaceous material is performed by grinding the slurry.
Claim 11
Independent Claim 223 words
A method of continuously forming discrete elongated tender protein filaments from proteinaceous material comprising: a. forming a pumpable slurry of a mixture of a protein containing material and an added material selected from the group consisting of cellulose and carbohydrate by-products from the processing of protein containing vegetable materials and grains; the slurry having a solids content above about 20% by weight and a protein content of above about 40% by weight on a dry basis, b. hydrating the proteinaceous material in the slurry to place the proteinaceous material in a sufficiently reactive form to produce elongated protein filaments, c. forming discrete elongated protein filaments by continuously conducting the slurry under pressure through an injection zone whereby steam is injected into said slurry to heat the slurry and heating the slurry to a temperature which is less than that which will degrade the protein while the protein is subjected to such temperature for a sufficient period of time so that elongated tender filaments are separated from the remaining constituents of the slurry, continuously removing the heated slurry from said zone through an orifice and discharging the formed discrete elongated filaments and the remaining constituents of the slurry into a collecting zone, and d. in said collecting zone separating the tender protein filaments from the remaining constituents of the slurry and recovering said filaments.
Claim 12
Independent Claim 223 words
A method of continuously forming discrete elongated tender protein filaments from proteinaceous material comprising: a. forming a pumpable slurry of a mixture of a protein containing material and an added material selected from the group consisting of cellulose and carbohydrate by-products from the processing of protein containing vegetable materials and grains; the slurry having a solids content above about 20% by weight and a protein content of above about 40% by weight on a dry basis, b. hydrating the proteinaceous material in the slurry to place the proteinaceous material in a sufficiently reactive form to produce elongated protein filaments, c. forming discrete elongated protein filaments by continuously conducting the slurry under pressure through an injection zone whereby steam is injected into said slurry to heat the slurry and heating the slurry to a temperature which is less than that which will degrade the protein while the protein is subjected to such temperature for a sufficient period of time so that elongated tender filaments are separated from the remaining constituents of the slurry, continuously removing the heated slurry from said zone through an orifice and discharging the formed discrete elongated filaments and the remaining constituents of the slurry into a collecting zone, and d. in said collecting zone separating the tender protein filaments from the remaining constituents of the slurry and recovering said filaments.
Claim 13
Dependent Claim 21 words
The method of claim 10 wherein the slurry is processed at a steam pressure of between about 80 and 85 psig.
Claim 14
Dependent Claim 20 words
The method of claim 10 wherein the slurry is heated in the heat exchange zone to a temperature above 165*F.
Claim 15
Dependent Claim 11 words
The method of claim 10 wherein the added material is cellulose.
Claim 16
Dependent Claim 22 words
The method of claim 10 wherein the protein containing material is selected from the group consisting of soy protein, albumen and casein.
Claim 17
Independent Claim 227 words
A method for continuously forming discrete elongated tender protein filaments from proteinaceous material comprising: a. forming a pumpable slurry of a protein containing material and an added material selected from the group consisting of cellulose and carbohydrate by-products from the processing of protein containing vegetable matErials and grains; the slurry having a solids content of above about 20% by eight and a protein content of above about 40% by weight on a dry basis, b. hydrating the proteinaceous material in the slurry by adjusting the pH of the slurry to above about 4.5 to place the proteinaceous material in a sufficiently reactive form to produce elongated protein filaments, forming discrete elongated protein filaments by continuously conducting the proteinaceous slurry under pressure through a heat exchange zone and heating the slurry to a temperature above 240*F. and less than that which will degrade the protein while the protein is subjected to such temperature for a sufficient period of time so that elongated tender filaments are separated from the remaining constituents of the slurry, continuously removing the heated slurry from said zone through a back pressure creating orifice and discharging the formed discrete elongated filaments and remaining constituents of the slurry into a collecting zone, and d. in said collecting zone separating the tender elongated protein filaments from the remaining constituents of the slurry and recovering said discrete filaments.
Claim 18
Independent Claim 227 words
A method for continuously forming discrete elongated tender protein filaments from proteinaceous material comprising: a. forming a pumpable slurry of a protein containing material and an added material selected from the group consisting of cellulose and carbohydrate by-products from the processing of protein containing vegetable matErials and grains; the slurry having a solids content of above about 20% by eight and a protein content of above about 40% by weight on a dry basis, b. hydrating the proteinaceous material in the slurry by adjusting the pH of the slurry to above about 4.5 to place the proteinaceous material in a sufficiently reactive form to produce elongated protein filaments, forming discrete elongated protein filaments by continuously conducting the proteinaceous slurry under pressure through a heat exchange zone and heating the slurry to a temperature above 240*F. and less than that which will degrade the protein while the protein is subjected to such temperature for a sufficient period of time so that elongated tender filaments are separated from the remaining constituents of the slurry, continuously removing the heated slurry from said zone through a back pressure creating orifice and discharging the formed discrete elongated filaments and remaining constituents of the slurry into a collecting zone, and d. in said collecting zone separating the tender elongated protein filaments from the remaining constituents of the slurry and recovering said discrete filaments.

References Cited (Backward Citations)

US3047395A Cited
US3662671A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-10-06 1979-04-07 1979-10-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-10-06 1983-04-07 1983-10-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-10-06 1987-04-07 1987-10-07 $7700.00 Window Closed / Lapsed

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