GB741728A - Manufacture of regenerated cellulose structures from viscose - Google Patents

Manufacture of regenerated cellulose structures from viscose

Info

Publication number
GB741728A
GB741728A GB11992/52A GB1199252A GB741728A GB 741728 A GB741728 A GB 741728A GB 11992/52 A GB11992/52 A GB 11992/52A GB 1199252 A GB1199252 A GB 1199252A GB 741728 A GB741728 A GB 741728A
Authority
GB
United Kingdom
Prior art keywords
per cent
viscose
filaments
spun
glycol
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
GB11992/52A
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Publication of GB741728A publication Critical patent/GB741728A/en
Expired legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F2/00Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
    • D01F2/06Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof from viscose
    • D01F2/08Composition of the spinning solution or the bath
    • D01F2/10Addition to the spinning solution or spinning bath of substances which exert their effect equally well in either

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

In the production of regenerated cellulose filaments and other products from viscose, a compound of the formula RO-(CH2CH2O)n-R1 is added to the viscose, preferably in a proportion of 0.5 to 1.0 per cent, and the mixture is extruded into an acid coagulating bath which preferably contains up to 15 per cent of zinc sulphate. The compound should be at least one per cent soluble in 6 per cent aqueous sodium hydroxide solution and not more than 0.5 per cent soluble at room temperature in the particular coagulating bath employed. In the formula, R is an alkyl or aryl radical, n is 1-4 (preferably 1 or 2) and R1 is hydrogen or an alkyl or aryl radical. Preferably the coagulated filaments are treated in a secondary hot bath (which may be water or 1-3 per cent sulphuric acid at 50-100 DEG C.) and stretched before they are wound. The viscose used may contain 4-10 (preferably 5-7) per cent of cellulose and 4-9 (preferably 4-7) per cent of alkali, and may have a relatively high salt index. The viscose may be unripened; and the bath temperature is preferably 40-75 DEG C. Specified additives of the formula above include ethoxy-, butoxy-, phenoxy-, methoxyethoxy-, butoxyethoxy- and phenoxyethoxy ethanols, diethylglycol ether and 1-ethenyloxy-2-methoxyethylene. In an example an unripened viscose, in which 0.5 per cent of phenoxyethanol has been mixed for 3 hours at 17 DEG C. is spun into a primary aqueous coagulating bath containing 6.5 per cent of sulphuric acid, 17.8 per cent of sodium sulphate and 9.5 per cent of zinc sulphate at 60 DEG C., and the filaments are passed through a 2 per cent sulphuric acid bath at 98 DEG C., stretched 100 per cent and collected on a bobbin. In other examples viscoses containing some of the additives listed above are spun in a similar manner and, in addition, examples are given of the spinning of unripened viscoses containing compounds of the formul C2H5O-(C2H4O)3-H; C4H9O-(C2H4O)3-H; and C6H5O-(C2H4O)3-H. Polyethylene glycols, preferably of mol. wt. 300-1000, the amines referred to in Specification 654,083 and the diamines referred to in Specification 741,727 may be used in conjunction with the compounds of the formula given above. In an example a viscose modified with 0.5 per cent of butoxyethanol, 0.2 per cent of polyethylene glycol (M.W. = 300) and 0.1 per cent of cyclohexylamine is spun as in the first example. The filaments have low gel-swelling values, high tenacities, substantially noncrenulated surfaces and a high proportion of skin. For the purpose of comparison, particulars are given of certain physical properties of filaments spun from viscose containing ethoxyethylacetate, the di(chlorethyl) ether of ethylene glycol, glycol diacetate, glycol diformate, the mono(chlorethyl) ether of ethylene glycol, ethoxyethyl acrylate, butoxyethoxyethyl acetate, the acetate of the monomethyl ether of triethylene glycol and triethylene glycol dicaprylate. Specifications 652,741 and 685,843 and U.S.A. Specifications 2,040,712, 2,440,057, 2,511,699 and 2,536,014 also are referred to.
GB11992/52A 1951-05-29 1952-05-12 Manufacture of regenerated cellulose structures from viscose Expired GB741728A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US319179XA 1951-05-29 1951-05-29

Publications (1)

Publication Number Publication Date
GB741728A true GB741728A (en) 1955-12-14

Family

ID=21862095

Family Applications (1)

Application Number Title Priority Date Filing Date
GB11992/52A Expired GB741728A (en) 1951-05-29 1952-05-12 Manufacture of regenerated cellulose structures from viscose

Country Status (5)

Country Link
BE (1) BE523479A (en)
CH (1) CH319179A (en)
DE (1) DE1078277B (en)
FR (1) FR1116103A (en)
GB (1) GB741728A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2929730A (en) * 1955-12-05 1960-03-22 American Viscose Corp Preparing viscose rayon
US5358765A (en) * 1992-03-04 1994-10-25 Viskase Corporation Cellulosic article containing an olefinic oxide polymer and method of manufacture
US5470519A (en) * 1992-03-04 1995-11-28 Viskase Corporation Method of manufacturing a cellulosic article containing an olefinic oxide polymer

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL103242C (en) * 1955-03-18 1962-12-17

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH150872A (en) * 1930-12-01 1931-11-30 Chem Fab Vormals Sandoz Process for the production of structures from viscose.
DE695094C (en) * 1936-03-28 1940-08-16 I G Farbenindustrie Akt Ges Process for the production of artificial structures from cellulose
US2451558A (en) * 1944-11-06 1948-10-19 Rayonier Inc Chemically treated wood pulp and a method of producing a cellulosic product

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2929730A (en) * 1955-12-05 1960-03-22 American Viscose Corp Preparing viscose rayon
US5358765A (en) * 1992-03-04 1994-10-25 Viskase Corporation Cellulosic article containing an olefinic oxide polymer and method of manufacture
US5470519A (en) * 1992-03-04 1995-11-28 Viskase Corporation Method of manufacturing a cellulosic article containing an olefinic oxide polymer

Also Published As

Publication number Publication date
CH319179A (en) 1957-02-15
BE523479A (en)
FR1116103A (en) 1956-05-04
DE1078277B (en) 1960-03-24

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