US3124415A - hours - Google Patents
hours Download PDFInfo
- Publication number
- US3124415A US3124415A US3124415DA US3124415A US 3124415 A US3124415 A US 3124415A US 3124415D A US3124415D A US 3124415DA US 3124415 A US3124415 A US 3124415A
- Authority
- US
- United States
- Prior art keywords
- fibers
- polyvinyl alcohol
- room temperature
- sample
- hours
- 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
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/14—Monocomponent 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
-
- Y—GENERAL 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S8/00—Bleaching and dyeing; fluid treatment and chemical modification of textiles and fibers
- Y10S8/10—Polyvinyl halide esters or alcohol fiber modification
Definitions
- Claim. (Cl. 8-1301) This invention relates to the treatment of polyvinyl alcohol fibers and is more particularly concerned with the heat-treatment of such fibers.
- Heat-treatment of polyvinyl alcohol fibers is carried out to increase the crystallization of the molecules of polyvinyl alcohol and to promote the water-resistance and elasticity of the fibers.
- the fibers are heated only at a temperature above the second transition point for a specified time and no consideration is given to the speed of cooling of the fibers after the heat treatment.
- polyvinyl alcohol fibers will be influenced by the size and number of crystalline particles in the fibers. particles, the higher the strength and water-resistance of the fibers.
- polyvinyl alcohol fibers are to be used for making fishing nets and the. like, wherein fibers of a high knot strength are required, it is necessary to provide fibers of large crystalline particles. However, there is danger that the fibers will harden. Accordingly, problems are present in the production of polyvinyl alcohol fibers having desired characteristics of the type indicated which are not solved by'conventional heat-treating operations.
- polyvinyl alcohol fibers are first heat-treated only for a short time at a temperature above the second transition point but below the melting point, e.g. at 200 to 225 C., in accordance with known practice, and thefibers are then cooled under controlled temperature and time conditions.
- the time of cooling is long, the crystallinity will be increased but a portion of the polyvinyl alcohol molecules will be thermally decomposed and saturated or unsaturated carbonyl radicals will be produced and 'discoloration will occur.
- discoloration is prevented, and crystallinity and knot strength are increased, by slowly cooling the fibers by maintaining them at a temperature above the second transition point (85 Q), but not above 100 C., for a period of time up to two hours, preferably /z to 2 hours, and then allowing them to cool at room temperature, i.e. about 25 C. until they are at room tempera-' ture.
- the fibers are maintained at constant length until left at room temperature.
- the invention will be further understood by reference heated by immersion in a molten metal (lead) bath at 220 C. for 1.5 minutes and were then cooled by the following procedures, while under tension to maintain constant length.
- Sample No. 1 In substantially saturated Na SO solu- Thus, the larger the crystalline tion (as used for wet spinning) at 30 C. for 5 minutes, then left at room temperature.
- Sample No. 2 In substantially saturated Na SO solution at 10 C. for 5 minutes, then left at room temperature.
- Sample No. 3 In an oven at 110 C. for 10 minutes, then left at room temperature.
- Sample No. 4 In an oven at 110 C. for 1 minute, then left at room temperature.
- Sample No. 6 Immersed for 1 minute in a mixture of solid carbon dioxide and acetone, then left at room temperature.
- Sample No. 1 In an oven at 100 C. for 1 hour, then left at room temperature.
- Sample No. 2 In an oven at C. for 1 hour, then left at room temperature.
- Sample No. 3 In an oven at 60 C. for 1 hour, then left at room temperature.
- Sample No. 4 Left at room temperature immediately.
- EXAMPLE 3 Five samples of wet-spun polyvinyl alcohol fibers were heat-treated at. 225 C. for 15 minutes as described in Example 2 and they were then further treated at 100 C. for various periods of time as described below.
- Sample No. 1 Maintained in an oven at 100 C. for 2 hours, then left at room temperature.
- the process of this invention is applicable to all types of fibers derived from polyvinyl alcohol produced in conventional manner and subjected to conventional treatments and processing operations, such as acetalization, stretching, and the like.
- Such fibers are conventionally spun from spinning solutions by known wet and dry spinning techniques. Spinning techniques are described, for example, in Cline et al. US. Patent 2,610,360 and Osugi et a1. Patent 2,906,594. An especially preferred spinning technique is described in copending.
- the heat treating step which is combined with the controlled cooling step of this invention is carried out in conventional manner at a temperature above the second transition point but below the melting point, e.g. at 200 to 225 C., for a short time, e.g. 1 to 2 minutes.
- Heat treatment is effected in a molten metal bath or in a hot salt bath or even in heated air in accordance with known practice. Such heat treatment, and subsequent controlled cooling, is effected while maintaining the fibers under tension at a constant length in accordance with conventional techniques.
- Polyvinyl alcohol fibers having a high percentage of crystallinity and a high knot strength produced by heating polyvinyl alcohol fibers to a temperature above the second application Serial No. 336,166 of Tomonari et al., filed February 10, 1953. Typical processes of treating polypatents and applications.
- step-Wise cooling of said fibers by maintaining them at a temperature above the second transition point but at a maximum of about C. for a period of time up to 2 hours and then cooling the fibers to room temperature.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
Description
March 10, 1964 MASAMITSU NAGANO ETAL 3,124,415
POLYVINYL ALCOHOL FIBERS HAVING HIGH CRYSTALLINITY AND KNOT STRENGTH Filed Sept. 2 1960 5 HOURS 3 HOURS I HOUR 2 OJOU m0 uummvuc TEMPERATURE INVENTORS MASAMITSU NAGANO BYHIDEO TOKUMITSU ATTORNEY United States. Patent 3 124 415 PGLYVINY L ALCQI-IbL FIBERS HAVING HIGH CRYSTALLY AND KNOT STRENGTH v Masamitsn Nagano and HideoTolrnmitsn, ()kayama City,
Japan, assignors to Knrashiki Rayon C0,, Ltd, Kuraslriki-shi, .lapan, a corporation of Japan Filed Sept. 2, 1960, Ser. No. 53,671
1 Claim. (Cl. 8-1301) This invention relates to the treatment of polyvinyl alcohol fibers and is more particularly concerned with the heat-treatment of such fibers.
Heat-treatment of polyvinyl alcohol fibers is carried out to increase the crystallization of the molecules of polyvinyl alcohol and to promote the water-resistance and elasticity of the fibers. However, in accordance with the conventional heat-treating method. The fibers are heated only at a temperature above the second transition point for a specified time and no consideration is given to the speed of cooling of the fibers after the heat treatment.
The mechanical properties of polyvinyl alcohol fibers will be influenced by the size and number of crystalline particles in the fibers. particles, the higher the strength and water-resistance of the fibers. When polyvinyl alcohol fibers are to be used for making fishing nets and the. like, wherein fibers of a high knot strength are required, it is necessary to provide fibers of large crystalline particles. However, there is danger that the fibers will harden. Accordingly, problems are present in the production of polyvinyl alcohol fibers having desired characteristics of the type indicated which are not solved by'conventional heat-treating operations.
It is an object of the present invention to provide a process of heat-treating polyvinyl alcohol fibers to impart to them a high percentagecrystallinity in the form of large crystal particles and high knot strength.
In accordance with the present invention, polyvinyl alcohol fibers are first heat-treated only for a short time at a temperature above the second transition point but below the melting point, e.g. at 200 to 225 C., in accordance with known practice, and thefibers are then cooled under controlled temperature and time conditions. When the time of cooling is long, the crystallinity will be increased but a portion of the polyvinyl alcohol molecules will be thermally decomposed and saturated or unsaturated carbonyl radicals will be produced and 'discoloration will occur. In accordance with the invention, discoloration is prevented, and crystallinity and knot strength are increased, by slowly cooling the fibers by maintaining them at a temperature above the second transition point (85 Q), but not above 100 C., for a period of time up to two hours, preferably /z to 2 hours, and then allowing them to cool at room temperature, i.e. about 25 C. until they are at room tempera-' ture. During the heatetreatment and during the controlled'cooling of the process of this invention, the fibers are maintained at constant length until left at room temperature.
The invention will be further understood by reference heated by immersion in a molten metal (lead) bath at 220 C. for 1.5 minutes and were then cooled by the following procedures, while under tension to maintain constant length.
Sample No. 1: In substantially saturated Na SO solu- Thus, the larger the crystalline tion (as used for wet spinning) at 30 C. for 5 minutes, then left at room temperature.
Sample No. 2: In substantially saturated Na SO solution at 10 C. for 5 minutes, then left at room temperature.
Sample No. 3: In an oven at 110 C. for 10 minutes, then left at room temperature.
Sample No. 4: In an oven at 110 C. for 1 minute, then left at room temperature.
Sample No. 5: Immediately left at room temperature.
Sample No. 6: Immersed for 1 minute in a mixture of solid carbon dioxide and acetone, then left at room temperature.
When the mechanical properties and the percentage crystallinity of the fibers treated as described above were determined, the values set forth in Table 1 were obtained:
Table 1 Softening point in water Dry strength a s! denier) Percentage Crystallinity Fineness (denier) Four samples of wet-spun polyvinyl alcohol fibers were heated by immersion in a molten metal (lead) bath at 225 C. for 1.5 minutes and were then cooled at various temperatures as described below.
Sample No. 1: In an oven at 100 C. for 1 hour, then left at room temperature.
Sample No. 2: In an oven at C. for 1 hour, then left at room temperature.
7 Sample No. 3: In an oven at 60 C. for 1 hour, then left at room temperature. Sample No. 4: Left at room temperature immediately.
The properties of the thus-treated fibers were found to be as follows:
' Table 2 Wet Wet knot Softening Sample No. Fmeness strength strength point in (denier) (granis/ (grams/ Water denier) denier) 0) These tests show that slow cooling at a temperature above the second transition point C.) is effective to increase the wet knot strength and other properties.
EXAMPLE 3 Five samples of wet-spun polyvinyl alcohol fibers were heat-treated at. 225 C. for 15 minutes as described in Example 2 and they were then further treated at 100 C. for various periods of time as described below.
Sample No. 1: Maintained in an oven at 100 C. for 2 hours, then left at room temperature.
The results of tests upon the thus-treated fibers are set forth in the following table:
Table 3 Wet Wet knot Fineness strength strength Sample N o. (diener) (grams/ (grams/ denier) denier) These results show that it is desirable to effect slow cooling as a type of annealing for a prolonged period of time. However, the relationship between the degree of discoloration of the fibers and the annealing time and temperature are shown in the accompanying drawing. At temperatures of up to about 100 C., even when the fibers were treated for hours, there was no discoloration.
As previously indicated, the process of this invention is applicable to all types of fibers derived from polyvinyl alcohol produced in conventional manner and subjected to conventional treatments and processing operations, such as acetalization, stretching, and the like. Such fibers are conventionally spun from spinning solutions by known wet and dry spinning techniques. Spinning techniques are described, for example, in Cline et al. US. Patent 2,610,360 and Osugi et a1. Patent 2,906,594. An especially preferred spinning technique is described in copending As previously mentioned, the heat treating step which is combined with the controlled cooling step of this invention is carried out in conventional manner at a temperature above the second transition point but below the melting point, e.g. at 200 to 225 C., for a short time, e.g. 1 to 2 minutes. Heat treatment is effected in a molten metal bath or in a hot salt bath or even in heated air in accordance with known practice. Such heat treatment, and subsequent controlled cooling, is effected while maintaining the fibers under tension at a constant length in accordance with conventional techniques.
It will be understood that the conditions and the relative relationships set forthabov e which are illustrative of the invention are those preferred in carrying'out the process of the invention but it will be understood that other conditions and relationships may be used within the scope of the invention.
It will, therefore, be further understood that various changes and modifications may be made in the embodiments of the invention herein described without departing from the scope of the invention as defined in the appended claim. It is intended, therefore, that all matter contained in the foregoing description and in the drawing shall be interpreted as illustrative only and not as limitative of the invention.
We claim:
Polyvinyl alcohol fibers having a high percentage of crystallinity and a high knot strength produced by heating polyvinyl alcohol fibers to a temperature above the second application Serial No. 336,166 of Tomonari et al., filed February 10, 1953. Typical processes of treating polypatents and applications.
transition point but below the melting point and effecting step-Wise cooling of said fibers by maintaining them at a temperature above the second transition point but at a maximum of about C. for a period of time up to 2 hours and then cooling the fibers to room temperature.
References Cited in the file of this patent UNITED STATES PATENTS 2,514,088 Pinsky July 4, 1950 2,732,592 Tunnicliif et a1. Jan. 31, 1956 2,878,519 Wolinski Mar. 24, 1959 2,906,594 Osugi Sept. 29, 1959
Publications (1)
Publication Number | Publication Date |
---|---|
US3124415A true US3124415A (en) | 1964-03-10 |
Family
ID=3453861
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US3124415D Expired - Lifetime US3124415A (en) | hours |
Country Status (1)
Country | Link |
---|---|
US (1) | US3124415A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3492079A (en) * | 1964-04-22 | 1970-01-27 | Rhodiaceta | Acetalisation of polyvinyl alcohol yarns |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2514088A (en) * | 1948-07-23 | 1950-07-04 | Plax Corp | Heat-treatment for plastic articles |
US2732592A (en) * | 1956-01-31 | Extrusion of thermoplastic material | ||
US2878519A (en) * | 1955-02-11 | 1959-03-24 | Du Pont | Surface treatment of polyethylene structures |
US2906594A (en) * | 1955-12-21 | 1959-09-29 | Air Reduction | Polyvinyl alcohol filaments of improved dye affinity and method of preparation |
-
0
- US US3124415D patent/US3124415A/en not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2732592A (en) * | 1956-01-31 | Extrusion of thermoplastic material | ||
US2514088A (en) * | 1948-07-23 | 1950-07-04 | Plax Corp | Heat-treatment for plastic articles |
US2878519A (en) * | 1955-02-11 | 1959-03-24 | Du Pont | Surface treatment of polyethylene structures |
US2906594A (en) * | 1955-12-21 | 1959-09-29 | Air Reduction | Polyvinyl alcohol filaments of improved dye affinity and method of preparation |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3492079A (en) * | 1964-04-22 | 1970-01-27 | Rhodiaceta | Acetalisation of polyvinyl alcohol yarns |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3243335A (en) | Ceramic product and process of producing it | |
GB1183875A (en) | Process for improving the Strength Retention and Absorption Rate of Polyglycolic Acid Sutures | |
US3149016A (en) | Nucleated glass particle and process for making it | |
GB816987A (en) | Improvements in and relating to the production of polychlorotrifluoroethylene filaments | |
US3124415A (en) | hours | |
US2452130A (en) | Method of spinning high tenacity viscose rayon | |
US4098776A (en) | Poly(arylene sulfide) fibers | |
US2743994A (en) | Method of producing shaped articles from polymeric materials | |
US3107970A (en) | Process for the manufacture of high tenacity viscose rayon | |
GB1018851A (en) | Bulky isotactic polypropylene yarns | |
US2782089A (en) | Process of improving the heat stability of polythiourea threads by applying an epoxy compound | |
DE2015820B2 (en) | PROCESS FOR MANUFACTURING FEDES OR YARNS FROM CARBON OR GRAPHITE | |
US3426117A (en) | Method for treating acrylic composite fiber | |
US3088794A (en) | Process for spinning and drawing polyalkylene isophthalamides | |
US3449476A (en) | Process of stretching polyacrylonitrile filaments | |
US2897044A (en) | Production of artificial protein threads, fibres, filaments and the like | |
US2404665A (en) | Methods of hardening and tanning of artificial fibers made of protein | |
US1626454A (en) | Manufacture of artificial silk and the like from viscose solutions | |
SU1035106A1 (en) | Method for treating wool yarn with liquid ammonia | |
SU144446A1 (en) | The method of processing fibers from polyvinyl alcohol | |
US2525825A (en) | Process for making casein fibers for felting | |
DE972846C (en) | Process for the production of viscose artificial silk threads | |
GB954824A (en) | Process for the production of filamentary reinforcing material | |
GB549642A (en) | Improvements in the manufacture and production of artificial threads, filaments and the like | |
US1995732A (en) | Process of manufacturing cellulose acetate |