GB770089A - Production of amylose films - Google Patents

Production of amylose films

Info

Publication number
GB770089A
GB770089A GB11580/55A GB1158055A GB770089A GB 770089 A GB770089 A GB 770089A GB 11580/55 A GB11580/55 A GB 11580/55A GB 1158055 A GB1158055 A GB 1158055A GB 770089 A GB770089 A GB 770089A
Authority
GB
United Kingdom
Prior art keywords
per cent
amylose
temperature
solution
film
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB11580/55A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Cooperative Avebe UA
Original Assignee
Cooperative Avebe UA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Cooperative Avebe UA filed Critical Cooperative Avebe UA
Publication of GB770089A publication Critical patent/GB770089A/en
Expired legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23BPRESERVING, e.g. BY CANNING, MEAT, FISH, EGGS, FRUIT, VEGETABLES, EDIBLE SEEDS; CHEMICAL RIPENING OF FRUIT OR VEGETABLES; THE PRESERVED, RIPENED, OR CANNED PRODUCTS
    • A23B4/00General methods for preserving meat, sausages, fish or fish products
    • A23B4/10Coating with a protective layer; Compositions or apparatus therefor
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23PSHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P30/00Shaping or working of foodstuffs characterised by the process or apparatus
    • A23P30/10Moulding
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L3/00Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
    • C08L3/02Starch; Degradation products thereof, e.g. dextrin
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2303/00Characterised by the use of starch, amylose or amylopectin or of their derivatives or degradation products
    • C08J2303/02Starch; Degradation products thereof, e.g. dextrin

Abstract

Strong, pliable and transparent amylose films are produced by dissolving at least 5 per cent by weight of a starch carbohydrate, containing at least 50 per cent by weight of amylose, in water at a temperature of at least 120 DEG C. and preferably 140-165 DEG C., cooling the solution to below its boiling point, casting a film from the resulting clear solution on a support having a temperature higher than the gelation temperature of the solution, and afterwards drying and cooling the film on the support and stripping it from the support. The concentration of the amylose solution may be up to about 25 per cent and is preferably 10-20 per cent. The amylose may have an average molecular weight of about 120,000 and is preferably dispersed in water having a pH of about 7, to which up to 0.2 per cent of sodium sulphite may be added. The dispersion may be heated in an autoclave or by passing it through heated tubes for 5-8 minutes, prolonged heating at an unnecessarily high temperature being avoided to minimize degradation of the amylose. The casting temperature is preferably sufficiently high to evaporate part of the water before the solution gels. The drying air may have a temperature of 90-110 DEG C., provided it has a high relative humidity, e.g. between 40 and 80 per cent, at the end of the drying process and during cooling. The amylose should preferably be free from contaminants, e.g. magnesium sulphate introduced during the preparation of the amylose from starch, but should preferably contain 10-20 per cent of amylopectin. A plasticizer such as glycerol or sorbitol may also be present. In the example, an aqueous slurry containing 15 per cent by weight of amylose, 0.05 per cent of sodium sulphite and 5 per cent of glycerol is heated to 160 DEG C. in about 2 minutes and kept at that temperature for about 4 minutes by passing it through heated tubes. The resulting clear solution is cooled to about 95 DEG C., filtered at 95 DEG C., cast on to an endless travelling belt of chromium-plated steel having a temperature of about 85 DEG C. and dried in hot air having a temperature of 100 DEG C. and a relative humidity of about 65 per cent. The film is then cooled while still on the belt in air having a temperature of about 22 DEG C. and a relative humidity of about 100 per cent, and is finally stripped from the belt. The amylose film is suitable for application in the food industries, due to its digestibility.ALSO:Strong, pliable and transparent amylose films are produced by dissolving at least 5 per cent by weight of a starch carbohydrate, containing at least 50 per cent by weight of amylose, in water at a temperature of at least 120 DEG C. and preferably 140 DEG -165 DEG C., cooling the solution to below its boiling point, casting a film from the resulting clear solution on a support having a temperature higher than the gelation temperature of the solution, and afterwards drying and cooling the film on the support and stripping it from the support. The concentration of the amylose solution may be up to about 25 per cent and is preferably 10-20 per cent. The amylose may have an average molecular weight of about 120,000, and is preferably dispersed in water having a pH of about 7, to which up to 0,2 per cent of sodium sulphite may be added. The dispersion may be heated in an autoclave or by passing it through heated tubes for 5-8 minutes, prolonged heating at an unnecessarily high temperature being avoided to minimize degradation of the amylose. The casting temperature is preferably sufficiently high to evaporate part of the water before the solution gels. The drying air may have a temperature of 90 DEG -110 DEG C., provided it has a high relative humidity, e.g. between 40 and 80 per cent, at the end of the drying process and during cooling. The amylose should preferably be free from contaminants, e.g. magnesium sulphate introduced during the preparation of the amylose from starch, but should preferably contain 10-20 per cent of amylopectin. A plasticizer such as glycerol or sorbitol may also be present. In the example, an aqueous slurry containing 15 per cent by weight of amylose, 0,05 of sodium sulphite and 5 per cent of glycerol is heated to 160 DEG C. in about 2 minutes and kept at that temperature for about 4 minutes by passing it through heated tubes. The resulting clear solution is cooled to about 95 DEG C., filtered at 95 DEG C., cast on to an endless travelling belt of chromium-plated steel having a temperature of about 85 DEG C, and dried in hot air having a temperature of 100 DEG C. and a relative humidity of about 65 per cent. The film is then cooled while still on the belt in air having a temperature of about 22 DEG C. and a relative humidity of about 100 per cent, and is finally stripped from the belt. The amylose film is suitable for application in the food industries, due to its digestibility.
GB11580/55A 1954-04-22 1955-04-21 Production of amylose films Expired GB770089A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL770089X 1954-04-22

Publications (1)

Publication Number Publication Date
GB770089A true GB770089A (en) 1957-03-13

Family

ID=19827873

Family Applications (1)

Application Number Title Priority Date Filing Date
GB11580/55A Expired GB770089A (en) 1954-04-22 1955-04-21 Production of amylose films

Country Status (1)

Country Link
GB (1) GB770089A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3127393A (en) * 1964-03-31 Reaction of amide and triazine substi-
US3130081A (en) * 1960-12-23 1964-04-21 Nat Starch Chem Corp Limited stability amylose dispersions and method of preparation
US3312641A (en) * 1963-06-19 1967-04-04 Staley Mfg Co A E Polyvinyl alcohol plasticized amylose compositions
DE1292838B (en) * 1958-01-29 1969-04-17 Vaessen Schoemaker Holding Bv Process for the production of aqueous amylose solutions
US4490526A (en) * 1983-05-05 1984-12-25 Dynamit Nobel Ag Method for the modification of starch in the presence of solvents
US4985082A (en) * 1987-11-20 1991-01-15 Lafayette Applied Chemistry, Inc. Microporous granular starch matrix compositions
US5445678A (en) * 1991-05-29 1995-08-29 Whistler; Roy L. Subgranular crystalline starch as fat substitute
US5651828A (en) * 1994-09-30 1997-07-29 Lafayette Applied Chemistry, Inc. Fat substitute for processed foods

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3127393A (en) * 1964-03-31 Reaction of amide and triazine substi-
DE1292838B (en) * 1958-01-29 1969-04-17 Vaessen Schoemaker Holding Bv Process for the production of aqueous amylose solutions
US3130081A (en) * 1960-12-23 1964-04-21 Nat Starch Chem Corp Limited stability amylose dispersions and method of preparation
US3312641A (en) * 1963-06-19 1967-04-04 Staley Mfg Co A E Polyvinyl alcohol plasticized amylose compositions
US4490526A (en) * 1983-05-05 1984-12-25 Dynamit Nobel Ag Method for the modification of starch in the presence of solvents
US4985082A (en) * 1987-11-20 1991-01-15 Lafayette Applied Chemistry, Inc. Microporous granular starch matrix compositions
US5445678A (en) * 1991-05-29 1995-08-29 Whistler; Roy L. Subgranular crystalline starch as fat substitute
US5580390A (en) * 1991-05-29 1996-12-03 Whistler; Roy L. Subgranular crystalline starch as fat substitute
US5651828A (en) * 1994-09-30 1997-07-29 Lafayette Applied Chemistry, Inc. Fat substitute for processed foods

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