US759332A - Manufacture of filaments or films from viscose. - Google Patents
Manufacture of filaments or films from viscose. Download PDFInfo
- Publication number
- US759332A US759332A US16161203A US1903161612A US759332A US 759332 A US759332 A US 759332A US 16161203 A US16161203 A US 16161203A US 1903161612 A US1903161612 A US 1903161612A US 759332 A US759332 A US 759332A
- Authority
- US
- United States
- Prior art keywords
- filaments
- viscose
- manufacture
- films
- acid
- 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
Links
- 229920000297 Rayon Polymers 0.000 title description 6
- 238000004519 manufacturing process Methods 0.000 title description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 238000000034 method Methods 0.000 description 9
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000011593 sulfur Substances 0.000 description 4
- 229910052717 sulfur Inorganic materials 0.000 description 4
- 229920002955 Art silk Polymers 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000002932 luster Substances 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000002939 deleterious effect Effects 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- RZFBEFUNINJXRQ-UHFFFAOYSA-M sodium ethyl xanthate Chemical compound [Na+].CCOC([S-])=S RZFBEFUNINJXRQ-UHFFFAOYSA-M 0.000 description 1
- 235000019345 sodium thiosulphate Nutrition 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- DHCDFWKWKRSZHF-UHFFFAOYSA-L thiosulfate(2-) Chemical compound [O-]S([S-])(=O)=O DHCDFWKWKRSZHF-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C49/00—Blow-moulding, i.e. blowing a preform or parison to a desired shape within a mould; Apparatus therefor
- B29C49/42—Component parts, details or accessories; Auxiliary operations
- B29C49/46—Component parts, details or accessories; Auxiliary operations characterised by using particular environment or blow fluids other than air
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
- D04H1/04—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres having existing or potential cohesive properties, e.g. natural fibres, prestretched or fibrillated artificial fibres
- D04H1/28—Regenerated cellulose series
Definitions
- My invention is especially valuable in the manufacture of the filaments commercially known as artificial silk, and I would refer to Letters Patent of the United States No. 622, 087, dated March 28, 1899,and No. 716,778, dated December 23, 1902, as containing descriptions of typical and convenient methods of obtaining such filaments.
- My improved process is addressed to obviating these objectionable features; and it consists in subjecting the filaments, &c., to the action of steam in the presence of sulfurous acid.
- I may employ the sulfurous acid in gaseous form in conjunction with the steam, or I may proceed by first immersing the filaments in a solution containing aeid sulfite of soda to saturation and also containing, say, live to ten per cent. of ammonium sulfate. If this latter method be followed, the solution should preferably be heated to about 60 centigrade, and after the immersion the filaments are subjected to the action of steam.
- the steaming process is continued, say, from one to two hours, according to the thickness of the filaments or films, and in the case of the manufacture of lilaments such as those intended for artificial silk the filament should be placed under tension during the steaming.
- the process is particularly valuable in connection with the manufacture of artificial silk, where a number of very fine viscose filaments are twisted into a composite strand.
- residual caustic soda if not neutralized, tends to redissolve the surface of the individual filaments, which are liable then to agglomerate into one coarse thread.
- the finely-divided residual sulfur also tends to deposit on the surface and injure the luster.
- the reactions due to the methods above described may be stated as follows:
- the viscose compound is decomposed by heat, the sulfur contained therein is transformed into hyposulfite of soda, and the caustic soda resulting from the decomposition of the cellulose sodium Xanthate is neutralized by the sulfurous acid, whether this be used alone or contained in the acid sulfite salt.
- the acid of the ammonium salt has also a similar neutralizing action.
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Artificial Filaments (AREA)
Description
UNITED STATES Patented May 10, 1904.
PATENT OFFICE.
CHARLES N. WAITE, OF LANSDOVV NE, PENNSYLVANIA, ASSIGNOR TO GENERAL ARTIFICIAL SILK COMPANY, A CORPORATION OF DELA- WARE.
MANUFACTURE OF FILAMENTS OR FILMS FROM VISCOSE- SPECIFICATION forming part of Letters Patent No. 759,332, dated May 10, 1904.
Application fil d June 15, 1903. Serial No. 161,612. (No specimens.)
. following is a specification.
My invention is especially valuable in the manufacture of the filaments commercially known as artificial silk, and I would refer to Letters Patent of the United States No. 622, 087, dated March 28, 1899,and No. 716,778, dated December 23, 1902, as containing descriptions of typical and convenient methods of obtaining such filaments.
In processes of this character the viscose is forced through a perforated plate into a setting solution, whereby the filaments are gelatinized to the required degree, the ultimate and complete decomposition of the viscose compound being attained at a later stage. The usual method of finally decomposing such filaments is to as far as possible wash out the by-products with a brine solution and then to treat the filament with a dilute acid. It is found that notwithstanding this treatment the product is liable to retain caustic soda in quantity suflicient to attack the regenerated viscose and that also a percentage of free sulfur may remain, which impairs the luster and color of the material.
My improved process is addressed to obviating these objectionable features; and it consists in subjecting the filaments, &c., to the action of steam in the presence of sulfurous acid. I may employ the sulfurous acid in gaseous form in conjunction with the steam, or I may proceed by first immersing the filaments in a solution containing aeid sulfite of soda to saturation and also containing, say, live to ten per cent. of ammonium sulfate. If this latter method be followed, the solution should preferably be heated to about 60 centigrade, and after the immersion the filaments are subjected to the action of steam. In either instance the steaming process is continued, say, from one to two hours, according to the thickness of the filaments or films, and in the case of the manufacture of lilaments such as those intended for artificial silk the filament should be placed under tension during the steaming. The process is particularly valuable in connection with the manufacture of artificial silk, where a number of very fine viscose filaments are twisted into a composite strand. In this case residual caustic soda, if not neutralized, tends to redissolve the surface of the individual filaments, which are liable then to agglomerate into one coarse thread. The finely-divided residual sulfur also tends to deposit on the surface and injure the luster.
The reactions due to the methods above described may be stated as follows: The viscose compound is decomposed by heat, the sulfur contained therein is transformed into hyposulfite of soda, and the caustic soda resulting from the decomposition of the cellulose sodium Xanthate is neutralized by the sulfurous acid, whether this be used alone or contained in the acid sulfite salt. The acid of the ammonium salt has also a similar neutralizing action.
After steaming it is only necessary to wash the filaments and dry them.
I have found that by this method the tendency of the residual caustic soda to attack the regenerated cellulose is avoided and that the residual sulfur is converted into a colorless and soluble hyposulfite. Thus the harshness and inferior luster and color due to the presence of these deleterious ingrpdients is In Witness whereof I have hereunto signed my name, this 13th day of June, A. D. 1903, in the presence of tWo subscribing Witnesses.
CHARLES N. VAITE.
Witnesses:
JAMES H. BELL, M. K. TRUMBORE.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16161203A US759332A (en) | 1903-06-15 | 1903-06-15 | Manufacture of filaments or films from viscose. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US16161203A US759332A (en) | 1903-06-15 | 1903-06-15 | Manufacture of filaments or films from viscose. |
Publications (1)
Publication Number | Publication Date |
---|---|
US759332A true US759332A (en) | 1904-05-10 |
Family
ID=2827821
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US16161203A Expired - Lifetime US759332A (en) | 1903-06-15 | 1903-06-15 | Manufacture of filaments or films from viscose. |
Country Status (1)
Country | Link |
---|---|
US (1) | US759332A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2796319A (en) * | 1954-04-02 | 1957-06-18 | Schweizerische Viscose | Viscose spinning process |
US4145391A (en) * | 1976-11-26 | 1979-03-20 | Rhone Poulenc Textile | Cellulose fiber process |
US5849818A (en) * | 1993-06-03 | 1998-12-15 | Walles; Wilhelm E. | Skin sulfonated particles in matrices |
-
1903
- 1903-06-15 US US16161203A patent/US759332A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2796319A (en) * | 1954-04-02 | 1957-06-18 | Schweizerische Viscose | Viscose spinning process |
US4145391A (en) * | 1976-11-26 | 1979-03-20 | Rhone Poulenc Textile | Cellulose fiber process |
US5849818A (en) * | 1993-06-03 | 1998-12-15 | Walles; Wilhelm E. | Skin sulfonated particles in matrices |
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