GB1002621A - Regenerated cellulose filaments and staple fibers and their production - Google Patents

Regenerated cellulose filaments and staple fibers and their production

Info

Publication number
GB1002621A
GB1002621A GB19337/63A GB1933763A GB1002621A GB 1002621 A GB1002621 A GB 1002621A GB 19337/63 A GB19337/63 A GB 19337/63A GB 1933763 A GB1933763 A GB 1933763A GB 1002621 A GB1002621 A GB 1002621A
Authority
GB
United Kingdom
Prior art keywords
filaments
viscose
bath
grams
contain
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
GB19337/63A
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.)
Toyobo Co Ltd
Original Assignee
Toyobo Co Ltd
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 Toyobo Co Ltd filed Critical Toyobo Co Ltd
Publication of GB1002621A publication Critical patent/GB1002621A/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
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S264/00Plastic and nonmetallic article shaping or treating: processes
    • Y10S264/27Process of spinning viscose where viscose has high degree of polymerization

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

1,002,621. Spinning viscose. TOYO SPINNING CO. Ltd. May 15, 1963 [May 16, 1962], No. 19337/63. Heading B5B. Regenerated cellulose filaments are made by extruding viscose having a gamma number of at least 50 through a spinneret into an aqueous coagulating bath containing per litre 15 to 35 grams of sulphuric acid, 0À1 to 3 grams of zinc sulphate and not more than 100 grams of sodium sulphate to form gel filaments which are regenerated to only a very slight or a moderate degree, withdrawing the filaments from the bath in a condition wherein they have a residual gamma number less than that of the original viscose, but of at least 40, and, while they are still wet with bath liquid, causing the filaments to travel through air to to be stored in air, their period of residence and their temperature during this step in the process being such as to regenerate them further to such an extent that their residual gamma number is 20 to 35. The filaments are then stretched, and before, after or during stretching, the regeneration of the filaments is completed either in air or in a bath of dilute sulphuric acid. Alternatively the incompletely regenerated filaments may be stretched and cut into staple fibres, and the completion of the regeneration step effected in the latter. The gamma number of the viscose at the time it is spun may be 55 to 80. The coagulation bath may contain a monoamine. The cellulose in the viscose may have a D.P. of at least 300. The viscose may contain 3 to 8% of cellulose and 2 to 6% of sodium hydroxide. It may have a ball fall viscosity of at least 30 seconds. The temperature of the coagulating bath may be 15‹ to 35‹ C. The regeneration bath may contain 2 to 15 grams of sulphuric acid per litre and its temperature may be at least 60‹ C. Specification 915,356 is referred to.
GB19337/63A 1962-05-16 1963-05-15 Regenerated cellulose filaments and staple fibers and their production Expired GB1002621A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002562 1962-05-16

Publications (1)

Publication Number Publication Date
GB1002621A true GB1002621A (en) 1965-08-25

Family

ID=12015528

Family Applications (1)

Application Number Title Priority Date Filing Date
GB19337/63A Expired GB1002621A (en) 1962-05-16 1963-05-15 Regenerated cellulose filaments and staple fibers and their production

Country Status (5)

Country Link
US (1) US3324216A (en)
BE (1) BE632439A (en)
CH (1) CH431802A (en)
DE (1) DE1294590B (en)
GB (1) GB1002621A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6503371B1 (en) 1998-01-15 2003-01-07 Acordis Kelheim Gmbh Manufacture of cellulosic particles

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1021537A (en) * 1963-03-07 1966-03-02 Teijin Ltd Method of producing viscose rayon staple and a spinning apparatus for use in the method
DE1259499B (en) * 1964-07-31 1968-01-25 Glanzstoff Ag Process for the production of regenerated cellulose staple fibers
US3434913A (en) * 1964-12-28 1969-03-25 Fmc Corp Viscose rayon fiber and method of making same
NL134509C (en) * 1965-08-03
US3539678A (en) * 1967-08-14 1970-11-10 Teijin Ltd High speed spinning method of viscose rayon filaments having high wet modulus
IE31637L (en) * 1967-11-06 1968-05-15 Chimiotex Regenerated cellulose filaments
US3875141A (en) * 1968-02-16 1975-04-01 Chimiotex Regenerated cellulose filaments

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL47053C (en) * 1935-12-12
NL51932C (en) * 1937-11-23
DE946387C (en) * 1943-07-16 1956-08-02 Shozo Tachikawa Process for the production of rayon by spinning viscose
NL73733C (en) * 1948-11-23
NL103223C (en) * 1949-08-25
NL107330C (en) * 1951-07-31
US2699983A (en) * 1951-08-03 1955-01-18 Textile & Chem Res Co Ltd Production of viscose rayon
NL254946A (en) * 1959-08-18
FR1266099A (en) * 1959-08-18 1961-07-07 Courtaulds Inc Further development in the manufacture of regenerated cellulose filaments
US3128147A (en) * 1959-09-30 1964-04-07 Courtaulds Ltd Process for treating polynosic fibers and products obtained thereby
FR1285924A (en) * 1959-11-02 1962-03-02 Tachikawa Res Inst Process for spinning from high polymerization rayon to viscose
US3084021A (en) * 1960-02-29 1963-04-02 Morimoto Saichi Process for producing regenerated cellulose filaments
US3108849A (en) * 1960-10-27 1963-10-29 Mitsubishi Rayon Co Process for producing viscose regenerated cellulose fibers
BE624034A (en) * 1962-11-14

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6503371B1 (en) 1998-01-15 2003-01-07 Acordis Kelheim Gmbh Manufacture of cellulosic particles

Also Published As

Publication number Publication date
BE632439A (en)
US3324216A (en) 1967-06-06
CH431802A (en) 1967-03-15
DE1294590B (en) 1969-05-08

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