GB868901A - Filtration process for starch - Google Patents
Filtration process for starchInfo
- Publication number
- GB868901A GB868901A GB3194159A GB3194159A GB868901A GB 868901 A GB868901 A GB 868901A GB 3194159 A GB3194159 A GB 3194159A GB 3194159 A GB3194159 A GB 3194159A GB 868901 A GB868901 A GB 868901A
- Authority
- GB
- United Kingdom
- Prior art keywords
- slurry
- polyoxyethylene
- starch
- monolaurate
- compound
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B30/00—Preparation of starch, degraded or non-chemically modified starch, amylose, or amylopectin
- C08B30/08—Concentration of starch suspensions
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Edible Oils And Fats (AREA)
Abstract
The water content of a starch slurry is lowered to a level of 33-45% when the slurry is dewatered, by adding to the slurry a minor proportion of an oxyalkalene-containing compound having surface-active properties, which compound has the property of reducing the water content of the slurry below that which results from dewatering the slurry without the use of such a compound; and dewatering the slurry. The preferred amount of the compound is 0,1%, but from 0,02% may be added. The starch may be that derived from corn, wheat, potato, tapioca, sago or cassava and may be in the form of raw starch, lightly treated oxidized starch, heavily treated oxidized starch or thin boiling starches. The compounds may be divided into 12 groups in which the following substances are specified:-Group (1) Polyoxyethylene-dilaurate, -monolaurate, -monostearate, and polyoxyethylene esters of mixed fatty and resin acids; (2) Polyoxyethylene sorbitol-pentalaurate, -hexalaurate, -4,5 oleate, -tetraoleate, -tetra-tall oil, and -dilaurate; (3) Polyoxyethylene sorbitan-monostearate, -dilaurate, -trioleate, and -monolaurate; (4) Sorbitan monolaurate and mono-oleate; (5) Diethylene glycol monolaurate; (6) Glyceryl-monolaurate, -oleostearate,-monostearate, or-monoricinoleate; (7) Polyoxypropylene stearate; (8) Polyoxyethylene lauryl ether; (9) Polyxyethylene lauric acid laurate; (10) Glycerol mannitan laurate; (11) A condensation product of polyoxypropylene and polyoxyethylene; (12) Nonyl phenoxypolyoxyethanol.ALSO:The water content of a starch slurry is lowered to a level of 33-45% when the slurry is dewatered, by adding to the slurry a minor proportion of an oxyalkylene-containing compound having surface active properties, which compound has the property of reducing the water content of the slurry below that which results from dewatering the slurry without the use of such a compound; and dewatering the slurry. The preferred amount of the compound is 0,1%, but from 0,02% may be added. The starch may be that derived from corn, wheat, potato, tapioca, sago or cassova and may be in the form of raw starch, lightly treated oxidised starch, heavily treated oxidised starch or thin boiling starches. The compounds may be divided into 12 groups in which the following substances are specified:-Group (1) Polyoxyethylene-dilaurate, -mono-laurate, -monostearate, and polyoxyethylene esters of mixed fatty and resin acids. (2) Polyoxyethylene sorbitol-pentalaurate, -hexalaurate, -4,5 oleate, -tetraoleate, -tetra-tall oil, and -dilaurate. (3) Polyoxyethylene sorbitan-monostearate, -dilaurate,-trioleate, and -monolaurate. (4) Sorbitan monolaurate and monooleate. (5) Diethylene glycol monolaurate. (6) Glyceryl-monolaurate, -oleostearate, -monostearate, or -monoricinoleate. (7) Polyoxypropylene stearate. (8) Polyoxyethylene lauryl ether. (9) Polyoxyethylene lauric acid laurate. (10) Glycerol mannitan laurate. (11) A condensation product of polyoxypropylene and polyoxyethylene. (12) Nonyl phenoxypolyoxyethanol.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3194159A GB868901A (en) | 1959-09-18 | 1959-09-18 | Filtration process for starch |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3194159A GB868901A (en) | 1959-09-18 | 1959-09-18 | Filtration process for starch |
Publications (1)
Publication Number | Publication Date |
---|---|
GB868901A true GB868901A (en) | 1961-05-25 |
Family
ID=10330672
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3194159A Expired GB868901A (en) | 1959-09-18 | 1959-09-18 | Filtration process for starch |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB868901A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4238331A (en) * | 1976-11-01 | 1980-12-09 | The British Petroleum Company Limited | Process for treating sea water containing waxy lipids |
EP1761567B2 (en) † | 2004-06-09 | 2016-06-15 | Dutch Agricultural Development & Trading Company B.V. | Processing of cassava |
-
1959
- 1959-09-18 GB GB3194159A patent/GB868901A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4238331A (en) * | 1976-11-01 | 1980-12-09 | The British Petroleum Company Limited | Process for treating sea water containing waxy lipids |
EP1761567B2 (en) † | 2004-06-09 | 2016-06-15 | Dutch Agricultural Development & Trading Company B.V. | Processing of cassava |
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