GB1283763A - A PROCESS FOR DRY SPINNING POLY-gamma-METHYL GLUTAMATE FILAMENTS - Google Patents

A PROCESS FOR DRY SPINNING POLY-gamma-METHYL GLUTAMATE FILAMENTS

Info

Publication number
GB1283763A
GB1283763A GB4107969A GB4107969A GB1283763A GB 1283763 A GB1283763 A GB 1283763A GB 4107969 A GB4107969 A GB 4107969A GB 4107969 A GB4107969 A GB 4107969A GB 1283763 A GB1283763 A GB 1283763A
Authority
GB
United Kingdom
Prior art keywords
solvent
polymer
filaments
chlorinated aliphatic
poly
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
GB4107969A
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.)
NISSIN SPINNING CO Ltd
Ajinomoto Co Inc
Original Assignee
NISSIN SPINNING CO Ltd
Ajinomoto Co Inc
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 NISSIN SPINNING CO Ltd, Ajinomoto Co Inc filed Critical NISSIN SPINNING CO Ltd
Publication of GB1283763A publication Critical patent/GB1283763A/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
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/68Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyaminoacids or polypeptides

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

1283763 Poly-γ-methyl glutamate filaments AJINOMOTO CO Inc and NISSIN SPINNING CO Ltd 18 Aug 1969 [23 Aug 1968] 41079/69 Heading B5B [Also in Division C3] Poly-γ-methyl glutamate filaments are produced by extruding into a heated atmosphere a solution of the polymer in a solvent consisting of a mixture of a chlorinated aliphatic hydrocarbon which is a good solvent for the polymer and another chlorinated aliphatic hydrocarbon which is a non-solvent for the polymer and which has a boiling point higher than the good solvent. The good solvent, which should have a boiling point lower than the melting point or decomposition point of the filaments formed, may be methylene dichloride, chloroform, 1,2- dichloroethane 1,1,2-trichloroethane or tetrachloroethane and the non-solvent for the polymer may be 1,1-dichloroethane, 1,2-dichloroethylene, carbon tetrachloride, 1,1,1-trichloroethane, 1,2-dichloropropane, 1,3-dichloropropane or tetrachloroethylene. Trichloroethylene may also be used as a non-solvent, if a slightly higher proportion is used, relative to the good solvent, than with other non-solvents. The weight ratio of the non-solvent to the good solvent may be from 1 : 9 to 1 : 1. The coagulating ability of various non solvent chlorinated aliphatic hydrocarbons with respect to a solution of the polymer in a chlorinated aliphatic hydrocarbon which is a good solvent for the polymer is determined by measuring the number of C.C.S. of the non-solvent which when added dropwise with stirring to a solution consisting of 7À2 grams of poly-γ-methyl glutamate having a degree of polymerization of 2,500 and 28À2 CCS. of 1,2-dichloroethane at 20‹ C. causes the polymer solution to develop a white turbidity and gelation. In the experiments turbidity occurred when 13 to 85 CCS. of the non-solvent chlorinated aliphatic hydrocarbons were mixed with the polymer solution. Hence a non-solvent is defined as one having a coagulating ability in this test of less than or equal to 85 mls; the coagulating ability of a good solvent is very low and may be regarded as effectively infinite. In further experiments solutions of poly-γ- methyl glutamate in various mixtures of the solvent and non-solvent chlorinated aliphatic hydrocarbons were heated to 50‹ C. and extruded through a spinneret into a spinning cell containing air heated to 90‹C. The filaments thereby formed could be stretched at stretch ratios up to 2À25.
GB4107969A 1968-08-23 1969-08-18 A PROCESS FOR DRY SPINNING POLY-gamma-METHYL GLUTAMATE FILAMENTS Expired GB1283763A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5981468 1968-08-23

Publications (1)

Publication Number Publication Date
GB1283763A true GB1283763A (en) 1972-08-02

Family

ID=13124062

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4107969A Expired GB1283763A (en) 1968-08-23 1969-08-18 A PROCESS FOR DRY SPINNING POLY-gamma-METHYL GLUTAMATE FILAMENTS

Country Status (3)

Country Link
DE (1) DE1942585A1 (en)
FR (1) FR2016273A1 (en)
GB (1) GB1283763A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0674522B2 (en) * 1985-11-08 1994-09-21 味の素株式会社 Artificial hair

Also Published As

Publication number Publication date
FR2016273A1 (en) 1970-05-08
DE1942585A1 (en) 1970-03-26

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Legal Events

Date Code Title Description
PS Patent sealed
PLNP Patent lapsed through nonpayment of renewal fees