US2777775A - Production of artificial filaments, threads, and the like - Google Patents
Production of artificial filaments, threads, and the like Download PDFInfo
- Publication number
- US2777775A US2777775A US429640A US42964054A US2777775A US 2777775 A US2777775 A US 2777775A US 429640 A US429640 A US 429640A US 42964054 A US42964054 A US 42964054A US 2777775 A US2777775 A US 2777775A
- Authority
- US
- United States
- Prior art keywords
- viscose
- production
- filaments
- threads
- percent
- 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 - Lifetime
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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
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
- D01F2/06—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
- D01F2/08—Composition of the spinning solution or the bath
- D01F2/10—Addition to the spinning solution or spinning bath of substances which exert their effect equally well in either
Definitions
- the cellulose molecules of the skin are believed to be more highly orientated than those of the core.
- the object of the present invention is to obtain modified viscose filaments which have a skin substantially thicker 7 than is normally obtained.
- a process for the production of artificial filaments comprises extruding viscose containing at least 0.1 millimole cose of a diaryl thiourea having the general formula where R1 and R3 are hydrogen or aliphatic or aryl radicals and R2 and R4 are aryl radicals, into an aqueous coagulating bath containing sulphuric acid, sodium sulphate and zinc sulphate.
- the preferred minimum concentration for addition to the viscose is one millimole per 100 grams of.
- the coagulating bath preferably contains from /2 to 15 percent of zinc sulphate.
- the present invention also includes viscose containing at least 0.1 millimole per 100 grams of the viscose of a diaryl thiourea having The general formula wherein R1 and R3 are hydrogen or aliphatic or radicals and R2 and R4 are aryl radicals.
- the preferred diaryl thiourea for present invention is thiocarbanilide
- the filaments obtained by the use according to the Example Viscose containing 7.4 percent of cellulose, 7.0 percent of caustic soda and 1.1 percent of combined sulphur was prepared in the usual manner. 1.0 millimole per 100 grams of viscose of thiocarbanilide was added and the viscose was mixed for one hour. When the viscose was 48 hours old from the beginning of the mixing stage and had a salt figure of 5.7 it was ready for spinning.
- the filaments had a non-crenulated surface and the filaments were bean shaped in cross-section.
- the amount of skin was at least 50 percent greater than the amount What we claim is:
- Viscose containing at least 0.1 millimole per grams of the viscose of thiocarbanilide.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
Description
Jan. 15, 1957 H. EDWARDS ET L PRODUCTION OF ARTIFICIAL FILAMENTS, THREADS, AND T Filed May 15, 1954 HE LIKE 1 (l'laim. (Cl. 10t:165)
section or" the filaments under specific conditions with selected dyestuffs. In addition to the difference in dyeing afiiuity and in swelling property between the skin and core,
- the cellulose molecules of the skin are believed to be more highly orientated than those of the core.
The object of the present invention is to obtain modified viscose filaments which have a skin substantially thicker 7 than is normally obtained.
According to the present invention a process for the production of artificial filaments comprises extruding viscose containing at least 0.1 millimole cose of a diaryl thiourea having the general formula where R1 and R3 are hydrogen or aliphatic or aryl radicals and R2 and R4 are aryl radicals, into an aqueous coagulating bath containing sulphuric acid, sodium sulphate and zinc sulphate.
The preferred minimum concentration for addition to the viscose is one millimole per 100 grams of.
maximum concentration is 10 millimoles per 100 grams of viscose. a skin substantially thicker thiourea necessary to give a desired cross-sectional shape and a surface free from crenulations. The coagulating bath preferably contains from /2 to 15 percent of zinc sulphate.
The present invention also includes viscose containing at least 0.1 millimole per 100 grams of the viscose of a diaryl thiourea having The general formula wherein R1 and R3 are hydrogen or aliphatic or radicals and R2 and R4 are aryl radicals.
aryl 7 Patented Jan. 15, 1957 The preferred diaryl thiourea for present invention is thiocarbanilide In addition to the stantial increase in skin thickness the filaments obtained by the use according to the Example Viscose containing 7.4 percent of cellulose, 7.0 percent of caustic soda and 1.1 percent of combined sulphur was prepared in the usual manner. 1.0 millimole per 100 grams of viscose of thiocarbanilide was added and the viscose was mixed for one hour. When the viscose was 48 hours old from the beginning of the mixing stage and had a salt figure of 5.7 it was ready for spinning.
through a jet having 750 holes, each 0.003 inch in diameter, into an aqueous coagulating bath containing 9.5 percent of sulphuric acid, 20 percent of sodium sulphate and 4.5 percent of zinc sulphate to give a thread of 1550 denier and 750 filaments. The length of immersion in the bath was 24 inches and the temperature of the bath was 48 C. The thread was drawn from the bath at a rate of 28 metres per minute by a godet and then passed through a dilute sulphuric acid bath maintained at a temperature of C. to a second godet rotating at a higher speed than the first godet, to impart an 80 percent stretch to the thread. The thread was collected in a centrifugal spinning box rotating at 4000 revolutions per minute. The cake obtained was washed free from acid, a suitable finish was applied and the cake was dried.
The filaments had a non-crenulated surface and the filaments were bean shaped in cross-section. The amount of skin was at least 50 percent greater than the amount What we claim is:
Viscose containing at least 0.1 millimole per grams of the viscose of thiocarbanilide.
References Cited in the file of this patent UNITED STATES PATENTS 2,118,293 Brinker May 24, 1938 2,322,981 Ubbelohde June 29, 1943 2,435,295 Stasse Feb. 3, 1948
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB17617/53A GB748147A (en) | 1953-06-25 | 1953-06-25 | Improvements in and relating to the production of artificial filaments, threads and the like from viscose |
Publications (1)
Publication Number | Publication Date |
---|---|
US2777775A true US2777775A (en) | 1957-01-15 |
Family
ID=10098275
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US429640A Expired - Lifetime US2777775A (en) | 1953-06-25 | 1954-05-13 | Production of artificial filaments, threads, and the like |
Country Status (2)
Country | Link |
---|---|
US (1) | US2777775A (en) |
GB (1) | GB748147A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2875078A (en) * | 1955-08-22 | 1959-02-24 | Atlas Powder Co | Spinning of viscose |
US2876124A (en) * | 1955-08-22 | 1959-03-03 | Atlas Powder Co | Spinning of viscose |
US2912299A (en) * | 1954-09-03 | 1959-11-10 | Chimotex Sa | Process of spinning viscose containing thiodiglycol |
US2914375A (en) * | 1954-05-12 | 1959-11-24 | American Enka Corp | Manufacture of viscose thread |
US2941892A (en) * | 1955-01-31 | 1960-06-21 | Atlas Powder Co | Spinning of viscose |
US2953463A (en) * | 1951-06-30 | 1960-09-20 | Monsanto Chemicals | Fire-retardant cellulosic compositions and process for producing fire-retardant cellulosic structures therefrom |
US2970883A (en) * | 1956-01-16 | 1961-02-07 | American Enka Corp | Manufacture of viscose rayon |
US2971817A (en) * | 1955-06-29 | 1961-02-14 | American Viscose Corp | Producing all skin rayon |
US2979376A (en) * | 1955-06-29 | 1961-04-11 | American Viscose Corp | Production of rayon |
US2983572A (en) * | 1958-06-06 | 1961-05-09 | American Enka Corp | Manufacture of viscose rayon |
US3509931A (en) * | 1965-10-05 | 1970-05-05 | Continental Gummi Werke Ag | Fiber reinforcing belt for vehicle tires |
US5482776A (en) * | 1988-10-05 | 1996-01-09 | Asahi Kasei Kogyo Kabushiki Kaisha | Viscose rayon fiber having superior appearance |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2118293A (en) * | 1935-03-20 | 1938-05-24 | Frederic A Brinker | Thiocarbanilid derivative |
US2322981A (en) * | 1934-11-21 | 1943-06-29 | Ubbelohde Leo | Cellulose product |
US2435295A (en) * | 1945-05-18 | 1948-02-03 | Allied Chem & Dye Corp | Preparation of thiocarbanilide and its homologs |
-
1953
- 1953-06-25 GB GB17617/53A patent/GB748147A/en not_active Expired
-
1954
- 1954-05-13 US US429640A patent/US2777775A/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2322981A (en) * | 1934-11-21 | 1943-06-29 | Ubbelohde Leo | Cellulose product |
US2118293A (en) * | 1935-03-20 | 1938-05-24 | Frederic A Brinker | Thiocarbanilid derivative |
US2435295A (en) * | 1945-05-18 | 1948-02-03 | Allied Chem & Dye Corp | Preparation of thiocarbanilide and its homologs |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2953463A (en) * | 1951-06-30 | 1960-09-20 | Monsanto Chemicals | Fire-retardant cellulosic compositions and process for producing fire-retardant cellulosic structures therefrom |
US2914375A (en) * | 1954-05-12 | 1959-11-24 | American Enka Corp | Manufacture of viscose thread |
US2912299A (en) * | 1954-09-03 | 1959-11-10 | Chimotex Sa | Process of spinning viscose containing thiodiglycol |
US2941892A (en) * | 1955-01-31 | 1960-06-21 | Atlas Powder Co | Spinning of viscose |
US2971817A (en) * | 1955-06-29 | 1961-02-14 | American Viscose Corp | Producing all skin rayon |
US2979376A (en) * | 1955-06-29 | 1961-04-11 | American Viscose Corp | Production of rayon |
US2875078A (en) * | 1955-08-22 | 1959-02-24 | Atlas Powder Co | Spinning of viscose |
US2876124A (en) * | 1955-08-22 | 1959-03-03 | Atlas Powder Co | Spinning of viscose |
US2970883A (en) * | 1956-01-16 | 1961-02-07 | American Enka Corp | Manufacture of viscose rayon |
US2983572A (en) * | 1958-06-06 | 1961-05-09 | American Enka Corp | Manufacture of viscose rayon |
US3509931A (en) * | 1965-10-05 | 1970-05-05 | Continental Gummi Werke Ag | Fiber reinforcing belt for vehicle tires |
US5482776A (en) * | 1988-10-05 | 1996-01-09 | Asahi Kasei Kogyo Kabushiki Kaisha | Viscose rayon fiber having superior appearance |
Also Published As
Publication number | Publication date |
---|---|
GB748147A (en) | 1956-04-25 |
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