GB524090A - Manufacture of artificial fibres from protein material - Google Patents
Manufacture of artificial fibres from protein materialInfo
- Publication number
- GB524090A GB524090A GB2150/39A GB215039A GB524090A GB 524090 A GB524090 A GB 524090A GB 2150/39 A GB2150/39 A GB 2150/39A GB 215039 A GB215039 A GB 215039A GB 524090 A GB524090 A GB 524090A
- Authority
- GB
- United Kingdom
- Prior art keywords
- treatment
- solution
- dispersion
- viscosity
- bristles
- 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
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F4/00—Monocomponent artificial filaments or the like of proteins; Manufacture thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
Abstract
524,090. Artificial filaments, bristles &e. albumens. TRAILL, D., SEDDON, R. V., SEVER, W., and IMPERIAL CHEMICAL INDUSTRIES, Ltd. Jan. 21, 1939, Nos. 2150 and 18569. [Classes 2 (ii) and 2 (iii)] Artificial filaments, including bristles, are obtained by extrusion into a coagulating bath of a thixotropic viscous solution which has been made by maintaining at a temperature not below about 60 ‹C. a dispersion of ground-nut protein in dilute aqueous ammonia until an increase in natural viscosity at least of the order of 5-fold has been obtained. The protein content of the dispersion may be 10-25 per cent. and the ammonia concentration may be 0.5-1.0 per cent. The thermal treatment may be such that the viscosity attained is the same as that attained after 2.5-3.0 hours heating at 70‹C. The viscosity of the hot viscous solution or jelly obtained by the heat treatment may be reduced by a mechanical shearing treatment, and a similar treatment may be applied during the heat treatment to avoid the formation of a jelly. Dispersion of the protein in the aqueous ammonia may be assisted by mechanical homogenization and by warming to a temperature below 60 ‹C. The mechanical shearing may be effected by means of a colloid mill, emulsifier, or homogeniser. The temperature of extrusion is not necessarily the same as that of the heat treatment. The coagulating liquid may be a solution of sulphuric acid with or without sodium or ammonium sulphate. The fibres produced may be subjected to treatment with formaldehyde or other hardening agent and to treatment to increase their resistance to damage by wet treatment liquids. In an example, a heat treated ground-nut protein dispersion is cooled, aged, and spun into sulphuric acid solution. The thread is drawn without tension from the bath, then passed into formaldehyde solution and over stretching rolls. It is washed, dried, and cut into bristles. These are soaked in a solution of thionyl chloride in carbon tetrachloride. In another example, the thread after treatment with formaldehyde and drying is cut to bristles and these are soaked in saturated brine containing formaldehyde and hydrochloric acid. In another example, a ground-nut protein dispersion in ammonia solution is passed into a circulating device comprising an open reservoir, a constant delivery pump, a tube or jet type of homogeniser, a heating coil and a manometer attached to a conduit leading to the reservoir. The viscosity of the moving liquid is approximately a linear function of the pressure recorded by the manometer. The dispersion is first circulated for some time without heating. The homogeniser, heating coil and reservoir are then heated by means of hot water, and the circulation is continued until the desired increase in viscosity is attained. The cooled solution is extruded into a salt-acid bath and the filaments are wound at high speed. Specifications 492,677, 492,895, 495,332, 513,896 and 513,910 are referred to.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL54888D NL54888C (en) | 1939-01-21 | ||
BE459142D BE459142A (en) | 1939-01-21 | ||
GB2150/39A GB524090A (en) | 1939-01-21 | 1939-01-21 | Manufacture of artificial fibres from protein material |
US308102A US2340909A (en) | 1939-01-21 | 1939-12-07 | Manufacture of artificial fibers from protein material |
FR862996D FR862996A (en) | 1939-01-21 | 1940-01-20 | Manufacture of artificial fibers using proteins |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2150/39A GB524090A (en) | 1939-01-21 | 1939-01-21 | Manufacture of artificial fibres from protein material |
Publications (1)
Publication Number | Publication Date |
---|---|
GB524090A true GB524090A (en) | 1940-07-30 |
Family
ID=9734480
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2150/39A Expired GB524090A (en) | 1939-01-21 | 1939-01-21 | Manufacture of artificial fibres from protein material |
Country Status (5)
Country | Link |
---|---|
US (1) | US2340909A (en) |
BE (1) | BE459142A (en) |
FR (1) | FR862996A (en) |
GB (1) | GB524090A (en) |
NL (1) | NL54888C (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
NL64057C (en) * | 1943-04-12 | |||
BE458874A (en) * | 1943-10-20 | |||
GB580434A (en) * | 1944-09-06 | 1946-09-06 | Robin Hamilton Kendall Thomson | Improvements in or relating to the production of artificial insolubilised wet-spun protein filaments |
NL60806C (en) * | 1944-09-06 | |||
GB589978A (en) * | 1945-03-23 | 1947-07-04 | Walter Anderson Caldwell | Improvements in or relating to the production of viscous aqueous alkaline solutions of vegetable globulins |
US2525825A (en) * | 1948-01-23 | 1950-10-17 | Robert F Peterson | Process for making casein fibers for felting |
US2854345A (en) * | 1956-05-02 | 1958-09-30 | Corn Prod Refining Co | Manufacture of filaments, films, or the like from natural proteinaceous material |
DE1494601C3 (en) * | 1964-04-18 | 1973-01-04 | Farbwerke Hoechst Ag, Vormals Meister Lucius & Bruening, 6000 Frankfurt | Beta-polyamide threads and processes for their manufacture |
JPS59140860A (en) * | 1983-01-28 | 1984-08-13 | Nippon Suisan Kaisha Ltd | Preparation of dried fin-like food and equipment therefor |
-
0
- NL NL54888D patent/NL54888C/xx active
- BE BE459142D patent/BE459142A/xx unknown
-
1939
- 1939-01-21 GB GB2150/39A patent/GB524090A/en not_active Expired
- 1939-12-07 US US308102A patent/US2340909A/en not_active Expired - Lifetime
-
1940
- 1940-01-20 FR FR862996D patent/FR862996A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
BE459142A (en) | |
FR862996A (en) | 1941-03-20 |
US2340909A (en) | 1944-02-08 |
NL54888C (en) |
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