US3383447A - Method of manufacturing synthetic fibers of polyvinyl alcohol having good stable configuration and water solubility - Google Patents

Method of manufacturing synthetic fibers of polyvinyl alcohol having good stable configuration and water solubility Download PDF

Info

Publication number
US3383447A
US3383447A US358925A US35892564A US3383447A US 3383447 A US3383447 A US 3383447A US 358925 A US358925 A US 358925A US 35892564 A US35892564 A US 35892564A US 3383447 A US3383447 A US 3383447A
Authority
US
United States
Prior art keywords
fibers
water solubility
polyvinyl alcohol
filament
synthetic fibers
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
Application number
US358925A
Inventor
Onishi Shigekazu
Morita Eiichi
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.)
Kurashiki Rayon Co Ltd
Original Assignee
Kurashiki Rayon 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 Kurashiki Rayon Co Ltd filed Critical Kurashiki Rayon Co Ltd
Application granted granted Critical
Publication of US3383447A publication Critical patent/US3383447A/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • D01F6/02Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/14Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated alcohols, e.g. polyvinyl alcohol, or of their acetals or ketals

Definitions

  • ABSTRACT OF THE DISCLOSURE A process for the preparation of polyvinyl alcohol fibers having excellent dimensional stability and water solubility, comprising dry or semi-melt spinning an aqueous solution of polyvinyl alcohol having a concentration of greater than 30 percent by weight, adjusting the moisture content of the resultant fibers to a value between 50 and 120 percent by Weight, stretching said fibers to a ratio of from 1.1 to 3.0 at a temperature of from 0 C.
  • polyvinyl alcohol fibers are useful for base cloths in the manufacture of chemical laces.
  • the present invention relates to a method of manufacturing synthetic fibers of polyvinyl alcohol having good configuration stability and water solubility.
  • the fabrics made of easily water soluble synthetic fibers of PVA used for the base cloth for chemical laces have disadvantage of causing excessive elongation and contraction or swelling affected by the change of temperature and moisture if PVA fibers of unstable configuration are used for weaving the fabric so that such fabrics are not desirable for the manufacture of laces since the dimension stability of the fabric is low.
  • contrivances have been tried to improve the dimension stability by selecting the heat setting condition to a higher temperature and longer duration in the process of manufacturing synthetic fibers of PVA.
  • the water solubility becomes worse and in order to adjust such contradictory effects it was only one method of improving the PVA fibers to be used for the base fabric of chemical laces to properly regulate the condition of heat setting.
  • an aqueous solution of PVA having a higher concentration above 30% is spun by dry spinning or semi-melt spinning and the fiber thus obtained is subjected to a low temperature stretch under such conditions that the mois- 3,383,447 Patented May 14, 1968 ture content of the produced filament is 30-120%, preferably -90%, the ambient temperature at 0100 C., preferably nearabout room temperature, and the stretch ratio of 1.1-3.0, then drying the filament to moisture content of 420%, preferably about 10%, and subjecting it again to a low temperature stretch .of the stretch ratio of 2-6 times, preferably more or less 4 times, at a temperature "below the secondary transition temperature of 160 C., thereby forming a proper strain within the PVA filament, and then left under the constant length in order to set the strain and thus succeeded in the manufacture of synthetic fibers of PVA having excellent dimension stability and good water solubility by forming a suitable strain in the filament and by further setting the strain thus formed.
  • the low temperature stretch .of the first step is preferably performed at a temperature below C. for the purpose of preventing excessive coagulation of filament. At more than of moisture it is diflicult to provide uniform filament when stretched and at less than 50% it is substantially impossible to effect the second stage low temperature stretch so that it is not desirable for the purpose of improving the tenacity of the produced threads.
  • the stretch ratio higher than 3.0 is not desirable as it affects the second stage stretch and degrades the quality of products.
  • the second stage low temperature stretch at a temperature higher than C. considerably increases the crystallization of filament and consequently reduces the water solubility .of the produced threads and the moisture content of more than 20% reduces the solubility of the product, while at less than 4% the stretching becomes difiicult so that the tenacity of the produced thread is low and a suitable strain can not be produced within the filament and accordingly the solubility is not good.
  • the stretch ratio of 2-6 times is most suitable, and at higher than 6 times crystallinity becomes better to decrease solubility, whilst at less than 2 times proper strain can not be produced in the filament, thereby spoiling the solubility.
  • Example 1 A concentrated aqueous solution of PVA of 47% concentration having the average degree of polymerization of 1,700 was spun by means of a semi-melt spinning process and the filament thus obtained under the state of moisture content of 80% was stretched to 1.2 times at a lower temperature, then dried to the state of 10% moisture content and stretched at a low temperature of 100 C. to 4.0 times, then filament of 6.75 denier having strain therein was wound around a bobbin and left for 24 hours at a temperature of 20 C. and relative humidity of 65% to set the strain.
  • the PVA filament was obtained having dry tenacity 4.0 g./d., dry elongation 15%, and dissolving temperature in water 84 C., and also having good dimension stability and water solubility.
  • Example 2 An aqueous solution of PVA having the average degree of polymerization 1,700 and 43% concentration was spun by a dry spinning process and the filament thus obtained was stretched under the state of 90% moisture content to 1.2 times at a low temperature, then dried and reduced the moisture content to 12%, and subjected to the second heat stretch to 3.0 times at a low temperature of 100 C.
  • the filament thus obtained having inner strain was taken up around a bobbin and left for 24 hours under the condition of temperature at 20 C. and relative humidity 65%, thereby providing PVA filament of 300 denier having dry tenacity of 2.5 g./d., dry elongation 19.0% and melting point in water of 82 C. and having good dimen sion stability and water solubility.
  • Example 3 A concentrated aqueous solution of PVA of 43% con centration having average degree of polymerization 1,200 was spun by a dry spinning process and the filament thus obtained was stretched under the state of 100% moisture content to 1.2 times, then dried to reduce the moisture content to and it was stretched again to 4.0 times at a low temperature of 100 C., thus the filament having inner strain was taken up around a bobbin and left for 24 hours at C. and 55% relative humidity.
  • PVA filament had 300 denier and showed dry tenacity of 3.0 g./d., dry elongation 10.0% melting point in water 73 C. and good dimension stability and water solubility.
  • a process for the preparation of polyvinyl alcohol fibers having excellent dimensional stability and Water solubility comprising dry spinning an aqueous solution of polyvinyl alcohol having a concentration of greater than percent by weight, adjusting the moisture content .of
  • the resultant fibers to a value between and percent by weight, stretching said fibers to a ratio of from 1.1 to 3.0 at a temperature of from 0 C. to 100 C., drying such stretched fibers until the moisture content thereof is reduced to a value between 4 and 20 percent by weight, again stretching the said fibers to a ratio of from 2 to 6 at a temperature of less than C., maintaining the said fibers at the constant length and strain imparted thereto by the latter stretch, and thence setting such strain.

Description

United States Patent 3,383,447 METHOD OF MANUFACTURING SYNTHETIC FIBERS 0F POLYVINYL ALCOHOL HAV- ING GOOD STABLE CONFIGURATION AND WATER SOLUBILITY Shigekazu Onishi and Eiichi Morita, Okayama, Japan, assignors to Kuraslliki Rayon Company Limited, Kurashiki, Japan, a corporation of Japan No Drawing. Filed Apr. 10, 1964, Ser. No. 358,925 Claims priority, application Japan, Apr. 23, 1963, 38/20,843 3 Claims. (Cl. 264-205) ABSTRACT OF THE DISCLOSURE A process for the preparation of polyvinyl alcohol fibers having excellent dimensional stability and water solubility, comprising dry or semi-melt spinning an aqueous solution of polyvinyl alcohol having a concentration of greater than 30 percent by weight, adjusting the moisture content of the resultant fibers to a value between 50 and 120 percent by Weight, stretching said fibers to a ratio of from 1.1 to 3.0 at a temperature of from 0 C. to 100 C., drying such stretched fibers until the moisture content thereof is reduced to a value between 4 and 20 percent by weight, again stretching the said fibers to a ratio of from 2 to 6 at a temperature of less than 160 C., maintaining the said fibers at the constant length and strain imparted thereto by the latter stretch, and thence setting such strain. The resultant polyvinyl alcohol fibers are useful for base cloths in the manufacture of chemical laces.
The present invention relates to a method of manufacturing synthetic fibers of polyvinyl alcohol having good configuration stability and water solubility.
It has heretofore been well known to manufacture easily water soluble synthetic fibers of polyvinyl alcohol (hereinafter abridged as PVA) having the softening point of 7090 C. by dry spinning aqueous solution of PVA and by subjecting spun fibers, after dried, to the heat stretch under a high temperature of at least higher than 120 C. and heat setting at about 200 C.
The fabrics made of easily water soluble synthetic fibers of PVA used for the base cloth for chemical laces have disadvantage of causing excessive elongation and contraction or swelling affected by the change of temperature and moisture if PVA fibers of unstable configuration are used for weaving the fabric so that such fabrics are not desirable for the manufacture of laces since the dimension stability of the fabric is low. In order to avoid the above defects, contrivances have been tried to improve the dimension stability by selecting the heat setting condition to a higher temperature and longer duration in the process of manufacturing synthetic fibers of PVA. On the other hand, however, the water solubility becomes worse and in order to adjust such contradictory effects it was only one method of improving the PVA fibers to be used for the base fabric of chemical laces to properly regulate the condition of heat setting.
After numerous experiments and various investigations about the lower temperature stretch of synthetic fibers of PVA, the inventors have succeeded in producing synthetic fibers of PVA having excellent dimension stability and good water solubility by a method entirely different from heretofore usual methods.
According to the invention, it is characterized in that an aqueous solution of PVA having a higher concentration above 30% is spun by dry spinning or semi-melt spinning and the fiber thus obtained is subjected to a low temperature stretch under such conditions that the mois- 3,383,447 Patented May 14, 1968 ture content of the produced filament is 30-120%, preferably -90%, the ambient temperature at 0100 C., preferably nearabout room temperature, and the stretch ratio of 1.1-3.0, then drying the filament to moisture content of 420%, preferably about 10%, and subjecting it again to a low temperature stretch .of the stretch ratio of 2-6 times, preferably more or less 4 times, at a temperature "below the secondary transition temperature of 160 C., thereby forming a proper strain within the PVA filament, and then left under the constant length in order to set the strain and thus succeeded in the manufacture of synthetic fibers of PVA having excellent dimension stability and good water solubility by forming a suitable strain in the filament and by further setting the strain thus formed.
The low temperature stretch .of the first step is preferably performed at a temperature below C. for the purpose of preventing excessive coagulation of filament. At more than of moisture it is diflicult to provide uniform filament when stretched and at less than 50% it is substantially impossible to effect the second stage low temperature stretch so that it is not desirable for the purpose of improving the tenacity of the produced threads.
The stretch ratio higher than 3.0 is not desirable as it affects the second stage stretch and degrades the quality of products.
The second stage low temperature stretch at a temperature higher than C. considerably increases the crystallization of filament and consequently reduces the water solubility .of the produced threads and the moisture content of more than 20% reduces the solubility of the product, while at less than 4% the stretching becomes difiicult so that the tenacity of the produced thread is low and a suitable strain can not be produced within the filament and accordingly the solubility is not good. The stretch ratio of 2-6 times is most suitable, and at higher than 6 times crystallinity becomes better to decrease solubility, whilst at less than 2 times proper strain can not be produced in the filament, thereby spoiling the solubility.
In order to firmly set the strain formed in the filament after the low temperature stretch, it is preferable to wind the stretched filament around a bobbin to maintain the constant length and left for a long time in an atmosphere of room temperature.
The invention will now be explained more in detail by examples.
Example 1 A concentrated aqueous solution of PVA of 47% concentration having the average degree of polymerization of 1,700 was spun by means of a semi-melt spinning process and the filament thus obtained under the state of moisture content of 80% was stretched to 1.2 times at a lower temperature, then dried to the state of 10% moisture content and stretched at a low temperature of 100 C. to 4.0 times, then filament of 6.75 denier having strain therein was wound around a bobbin and left for 24 hours at a temperature of 20 C. and relative humidity of 65% to set the strain. Thus the PVA filament was obtained having dry tenacity 4.0 g./d., dry elongation 15%, and dissolving temperature in water 84 C., and also having good dimension stability and water solubility.
Example 2 An aqueous solution of PVA having the average degree of polymerization 1,700 and 43% concentration was spun by a dry spinning process and the filament thus obtained was stretched under the state of 90% moisture content to 1.2 times at a low temperature, then dried and reduced the moisture content to 12%, and subjected to the second heat stretch to 3.0 times at a low temperature of 100 C. The filament thus obtained having inner strain was taken up around a bobbin and left for 24 hours under the condition of temperature at 20 C. and relative humidity 65%, thereby providing PVA filament of 300 denier having dry tenacity of 2.5 g./d., dry elongation 19.0% and melting point in water of 82 C. and having good dimen sion stability and water solubility.
Example 3 A concentrated aqueous solution of PVA of 43% con centration having average degree of polymerization 1,200 was spun by a dry spinning process and the filament thus obtained was stretched under the state of 100% moisture content to 1.2 times, then dried to reduce the moisture content to and it was stretched again to 4.0 times at a low temperature of 100 C., thus the filament having inner strain was taken up around a bobbin and left for 24 hours at C. and 55% relative humidity.
Thus obtained PVA filament had 300 denier and showed dry tenacity of 3.0 g./d., dry elongation 10.0% melting point in water 73 C. and good dimension stability and water solubility.
What we claim is:
1. A process for the preparation of polyvinyl alcohol fibers having excellent dimensional stability and Water solubility, comprising dry spinning an aqueous solution of polyvinyl alcohol having a concentration of greater than percent by weight, adjusting the moisture content .of
the resultant fibers to a value between and percent by weight, stretching said fibers to a ratio of from 1.1 to 3.0 at a temperature of from 0 C. to 100 C., drying such stretched fibers until the moisture content thereof is reduced to a value between 4 and 20 percent by weight, again stretching the said fibers to a ratio of from 2 to 6 at a temperature of less than C., maintaining the said fibers at the constant length and strain imparted thereto by the latter stretch, and thence setting such strain.
2. The process as defined by claim 1, wherein the moisture content of the fibers is adjusted to a value between 80 and 90 percent by weight, the stretched fibers are dried until the moisture content thereof is reduced to a value of about 10 percent by weight, and further wherein the latter stretch is to a ratio of about 4.
3. The process as defined by claim 1, wherein the strain is set by maintaining the said fibers at constant length for at least 24 hours under ambient conditions.
References Cited UNITED STATES PATENTS 2,146,295 2/1939 Herrmann et a1. 264 2,610,359 9/1952 Hatchard et al 2642l0 2,610,360 9/1952 Cline et al 264-210 3,066,999 12/1962 Nakojo et al 264-210 3,238,283 3/1966 Fujii et al 264--210 DONALD J. ARNOLD, Primary Examiner.
US358925A 1963-04-23 1964-04-10 Method of manufacturing synthetic fibers of polyvinyl alcohol having good stable configuration and water solubility Expired - Lifetime US3383447A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2084363 1963-04-23

Publications (1)

Publication Number Publication Date
US3383447A true US3383447A (en) 1968-05-14

Family

ID=12038337

Family Applications (1)

Application Number Title Priority Date Filing Date
US358925A Expired - Lifetime US3383447A (en) 1963-04-23 1964-04-10 Method of manufacturing synthetic fibers of polyvinyl alcohol having good stable configuration and water solubility

Country Status (4)

Country Link
US (1) US3383447A (en)
AT (1) AT248604B (en)
CH (1) CH437625A (en)
GB (1) GB1049696A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3514460A (en) * 1963-12-17 1970-05-26 British Nylon Spinners Ltd Process of drawing nub-free polyamide yarn
US4942089A (en) * 1985-11-01 1990-07-17 Kuraray Company Limited Rapidly shrinking fiber and water-absorbing shrinkable yarn and other materials comprising same
CN111101220A (en) * 2018-10-26 2020-05-05 中国石油化工股份有限公司 Sand-impregnated vinylon and method for preparing sand-impregnated vinylon by dry spinning

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110331457B (en) * 2019-07-15 2021-12-07 安徽皖维高新材料股份有限公司 Method for preparing low-temperature polyvinyl alcohol water-soluble fiber

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2146295A (en) * 1931-03-10 1939-02-07 Chemische Forschungs Gmbh Polymerized vinyl alcohol articles and process of making same
US2610359A (en) * 1950-04-22 1952-09-16 Du Pont Process for producing polyvinyl alcohol filaments of improved properties
US2610360A (en) * 1950-04-22 1952-09-16 Du Pont Water-resistant polyvinyl alcohol filament and process for producing same
US3066999A (en) * 1958-08-19 1962-12-04 Kurashiki Rayon Co Polyvinyl alcohol fiber and method of making the same
US3238283A (en) * 1960-11-29 1966-03-01 Kurashiki Rayon Co Methods of producing shaped products of polyvinyl alcohol

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2146295A (en) * 1931-03-10 1939-02-07 Chemische Forschungs Gmbh Polymerized vinyl alcohol articles and process of making same
US2610359A (en) * 1950-04-22 1952-09-16 Du Pont Process for producing polyvinyl alcohol filaments of improved properties
US2610360A (en) * 1950-04-22 1952-09-16 Du Pont Water-resistant polyvinyl alcohol filament and process for producing same
US3066999A (en) * 1958-08-19 1962-12-04 Kurashiki Rayon Co Polyvinyl alcohol fiber and method of making the same
US3238283A (en) * 1960-11-29 1966-03-01 Kurashiki Rayon Co Methods of producing shaped products of polyvinyl alcohol

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3514460A (en) * 1963-12-17 1970-05-26 British Nylon Spinners Ltd Process of drawing nub-free polyamide yarn
US4942089A (en) * 1985-11-01 1990-07-17 Kuraray Company Limited Rapidly shrinking fiber and water-absorbing shrinkable yarn and other materials comprising same
CN111101220A (en) * 2018-10-26 2020-05-05 中国石油化工股份有限公司 Sand-impregnated vinylon and method for preparing sand-impregnated vinylon by dry spinning

Also Published As

Publication number Publication date
DE1435523B2 (en) 1973-02-01
AT248604B (en) 1966-08-10
GB1049696A (en) 1966-11-30
CH437625A (en) 1967-06-15
DE1435523A1 (en) 1968-11-21

Similar Documents

Publication Publication Date Title
US2346208A (en) Treatment of high tenacity yarn of synthetic origin
US2715763A (en) Synthetic textile fiber
US2312152A (en) Rayon and method of manufacturing same
US2716049A (en) Water-soluble yarn
KR930002568A (en) Highly aging resistant industrial fabric with controlled breathability and manufacturing method thereof
JPH03167309A (en) Fiber, filament and yarn based on cellulose and polyvinyl chloride and production thereof
US3383447A (en) Method of manufacturing synthetic fibers of polyvinyl alcohol having good stable configuration and water solubility
JPS6233327B2 (en)
US4067948A (en) Process for the production of high-shrinkage wet-spun acrylic fibres or filaments
US5109092A (en) Filaments and fibers of acryling polymers which contain carboxyl groups and process for their production
US4205037A (en) Process for producing acrylic synthetic fibers having anti-pilling properties
US2805464A (en) Fiber treatment
US2636804A (en) Process of treating polyvinyl alcohol fibers
US4447384A (en) Process for producing antipilling acrylic synthetic fiber
US3111366A (en) Method for producing high shrinking acrylonitrile polymer fibres
US1921426A (en) Method of treating artificial silk
US3404204A (en) Method of producing high-shrinkage acrylic fibers
US3120095A (en) Method of making high bulk yarns
US3083071A (en) Treatment of synthetic fiber tow
US3101245A (en) Production of polyacrylonitrile fibers
US2499477A (en) Vinyl resin textile article
US3689621A (en) Continuous wet spinning method of producing useful filamentary materials of an acrylonitrile copolymer
US1959350A (en) Manufacture or treatment of textile or other material
US2733121A (en) R in wash liquor
US2888317A (en) Production of polyacrylonitrile filaments of high uniform density