CN101117735A - Sub-patterned polyphenylene sulfide fibre manufacturing technology and equipment - Google Patents
Sub-patterned polyphenylene sulfide fibre manufacturing technology and equipment Download PDFInfo
- Publication number
- CN101117735A CN101117735A CNA2007100128607A CN200710012860A CN101117735A CN 101117735 A CN101117735 A CN 101117735A CN A2007100128607 A CNA2007100128607 A CN A2007100128607A CN 200710012860 A CN200710012860 A CN 200710012860A CN 101117735 A CN101117735 A CN 101117735A
- Authority
- CN
- China
- Prior art keywords
- polyphenylene sulfide
- sub
- solid
- production
- fiber
- 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.)
- Pending
Links
Abstract
A technology and an equipment for manufacturing of sub-linear polyphenylene sulfide fiber belong to the research and development field of manufacturing technology and equipment of sub-linear polyphenylene sulfide fiber. Using injection-grade polyphenylene sulfide resin as the raw production material, the present invention, with solid polymerization, obtains excellent silk-forming property by uniformly distributing the molecular weight of molten raw-material bodies and bettering the flowability. The equipment of the present invention adopts a common spinning fiber production line, wherein the back part of a material feed hopper has a solid polymerizer, the front and rear parts of which respectively have a material inlet screw and a material outlet screw for controlling the amount of feeding and discharging material. The method of the present invention can be easily implemented; the object of producing sub-linear fiber with raw material of injection-grade resin can be realized just by slightly modifying a common spinning production line and controlling the polymerization temperature and pressure in production. The method solves the fiber production vacancy of the prior art and expands the raw material source for polyphenylene sulfide fiber production, and therefore being an ideal method for production of sub-linear polyphenylene sulfide fiber.
Description
Technical field
The invention belongs to the manufacturing technology of sub-patterned polyphenylene sulfide fibre and the research and development field of equipment.
Background technology
Polyphenylene sulfide fibre is by the polyphenylene sulfide manufacturing, and polyphenylene sulfide is divided into high linear and low linear according to molecular structure, be called fibre-grade on the market with two kinds of injection grade.Generally can make polyphenylene sulfide fibre, and that the polyphenylene sulfide of injection grade can only be used for is plastic injection-moulded, can not makes polyphenylene sulfide fibre with the fiber-grade polyphenyl thioether resin.Because the molecular weight distribution inequality of injection grade polyphenylene sulfide melt is mobile bad unstable again, so be not easy into silk.Therefore the injection grade resin can not producd fibers.Because fibre-grade is different with the injection grade resin property different with manufacturing cost, so their price variance is very big, fibre resin is the twice of injection grade resin.Sub-patterned polyphenylene sulfide fibre manufacturing technology is exactly to adopt the polyphenylene sulfide of injection grade to make polyphenylene sulfide fibre.To reduce production costs, widen and produce the polyphenylene sulfide fibre raw material sources.
Summary of the invention
The purpose of this invention is to provide a kind of skill that adopts the injection grade polyphenylene sulfide to make fiber
Art and equipment are with the breakthrough that realizes that the injection grade raw material can be made fiber.
The present invention is achieved by the following scheme
Earlier the polyphenylene sulfide resin fat raw material with injection grade carries out solid phase, behind solid phase, enters screw extruder, manifold is produced.
Its device structure is:
Have a solid-phase aggregator at the rear portion of spinning production line loading hopper.Between loading hopper and solid-phase aggregator, have feed worm.At the rear portion of solid-phase aggregator is spinning manifold.Between solid-phase aggregator and spinning manifold, have the discharging screw rod.Loading hopper, feed worm, solid-phase aggregator, discharging screw rod, spinning manifold interconnect by pipeline.
Its production method is:
Resin raw material enters solid-phase aggregator from loading hopper and carries out solid phase, and the temperature of solid phase is between 240~260 ℃, and temperature is remained on more than the polyphenylene sulfide softening temperature.Negative-pressure vacuum degree in the solid-phase aggregator is 400~500mmhg.Polymerization time is 4~5 hours.Feed worm on the equipment and discharging screw rod are to be used for controlling the amount of charging and the amount of discharging.The program of its production is: the solid phase fusion, to extrude, spray silk moulding integrated, the bucket that falls then, and boundling, drawing-off is curled, drying, typing is cut off, packing.Finish production process.
Key problem in technology of the present invention is to have solved the problem that injection grade molecular resin amount increases.Because more than softening point, so when extrusion molten, fusion is even, the good fluidity of melt, thus it is irregular to have overcome injection grade polyphenylene sulfide melt molecular weight distribution, and flowing instability is difficult for becoming the shortcoming of silk.The inventive method is simple, and is easy to implement, just common VD404 spinning production line transformed a little, grasps the temperature and pressure of solid phase in the production, can reach to adopt the injection grade resin raw material to produce the polyphenylene sulfide fibre effect.Realize the production of sub-patterned polyphenylene sulfide fibre.Solved the problem that the injection grade resin can not producd fibers.Widened the source of polyphenylene sulfide fibre raw materials for production.Be a kind of desirable sub-patterned polyphenylene sulfide fibre manufacturing technology and equipment.
Description of drawings
Accompanying drawing is the present device structure chart
1-loading hopper 2-feed worm 3-solid-phase aggregator 4-discharging screw rod 5-spinning manifold
The specific embodiment
Embodiment 1
The present device structure has a solid-phase aggregator (3) at the rear portion of loading hopper (1) as shown in drawings.Between loading hopper and solid-phase aggregator, have feed worm (2).At the rear portion of solid-phase aggregator is spinning manifold (5).Between solid-phase aggregator and spinning manifold, have discharging screw rod (4).Loading hopper, feed worm, solid-phase aggregator, discharging screw rod, spinning manifold interconnect by pipeline.
Embodiment 2
Resin raw material enters solid-phase aggregator from loading hopper and carries out solid phase, and the temperature of solid phase is at 240 ℃, and the negative-pressure vacuum degree in the solid-phase aggregator is 400mmhg.Polymerization time is 4 hours.
The extrusion pressure of screw rod is 80kg/cm
2, each distinguishes temperature between 295~330 ℃.
The predraft multiple of spinning is more than 80 times, more than the spinning speed 400m/min.
Draw ratio during drawing-off adopts the present invention can produce desirable polyphenylene sulfide fibre more than 3.5.
Embodiment 3
Resin raw material enters solid-phase aggregator from loading hopper and carries out solid phase, and the temperature of solid phase is at 250 ℃, and the negative-pressure vacuum degree in the solid-phase aggregator is 500mmhg.Polymerization time is 5 hours.
Claims (2)
1. sub-patterned polyphenylene sulfide fibre manufacturing technology is characterized in that; The temperature of solid phase is between 240~260 ℃, and the negative-pressure vacuum degree in the solid-phase aggregator is 400~500mmhg, and polymerization time is 4~5 hours.
2. sub-patterned polyphenylene sulfide fibre manufacturing equipment, it is characterized in that: have a solid-phase aggregator at the rear portion of spinning production line loading hopper, between loading hopper and solid-phase aggregator, have feed worm, at the rear portion of solid-phase aggregator is spinning manifold, has the discharging screw rod between solid-phase aggregator and spinning manifold.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2007100128607A CN101117735A (en) | 2007-09-14 | 2007-09-14 | Sub-patterned polyphenylene sulfide fibre manufacturing technology and equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2007100128607A CN101117735A (en) | 2007-09-14 | 2007-09-14 | Sub-patterned polyphenylene sulfide fibre manufacturing technology and equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101117735A true CN101117735A (en) | 2008-02-06 |
Family
ID=39053991
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNA2007100128607A Pending CN101117735A (en) | 2007-09-14 | 2007-09-14 | Sub-patterned polyphenylene sulfide fibre manufacturing technology and equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101117735A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103088461A (en) * | 2013-01-27 | 2013-05-08 | 陈逊 | Manufacturing process of polyphenylene sulfide macrofiber |
CN105463592A (en) * | 2010-09-09 | 2016-04-06 | 松下知识产权经营株式会社 | Nanofiber manufacturing apparatus and nanofiber manufacturing method |
-
2007
- 2007-09-14 CN CNA2007100128607A patent/CN101117735A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105463592A (en) * | 2010-09-09 | 2016-04-06 | 松下知识产权经营株式会社 | Nanofiber manufacturing apparatus and nanofiber manufacturing method |
CN105463592B (en) * | 2010-09-09 | 2017-12-22 | 松下知识产权经营株式会社 | Nano-fiber manufacturing apparatus and nanofiber manufacture method |
CN103088461A (en) * | 2013-01-27 | 2013-05-08 | 陈逊 | Manufacturing process of polyphenylene sulfide macrofiber |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103497484B (en) | Gao Mo, high-strength, high heat-resisting polyformaldehyde composite material and preparation method thereof | |
CN103522518B (en) | Multifunctional wood-plastic composite material one-step method extruder | |
CN103571039A (en) | High-melt index polypropylene composition and preparation method thereof | |
CN203580087U (en) | Twin-screw extruder for differential nano material | |
CN103030891A (en) | Long glass fiber-reinforced polypropylene composite material and preparation method thereof | |
CN109575557B (en) | PC/ABS mixture for three-dimensional printing, preparation method thereof and direct printing method | |
CN102729450B (en) | The preparation facilities of fiber reinforced thermoplastic resin composite board/sheet material and method | |
CN103726126A (en) | Method for producing flat filament by using PET (Polyethylene Terephthalate) | |
CN103381662A (en) | Long and short fiber composite strengthening thermoplastic plastic particle material and production method thereof | |
CN101117735A (en) | Sub-patterned polyphenylene sulfide fibre manufacturing technology and equipment | |
CN202037848U (en) | Extruder for pipette | |
CN101602251B (en) | Method for producing elbow using polyethylene pipe and producing apparatus | |
CN204434906U (en) | A kind of equipment for spun-bonded non-woven | |
CN204658906U (en) | A kind of combination of the twin-screw for glass fiber reinforcement PC | |
CN209079104U (en) | A kind of injection mold convenient for charging | |
CN115216088B (en) | Light-weight modification method of plastic and modified product | |
CN204800983U (en) | Combined material , special former of high -molecular polymer material | |
CN203580086U (en) | Extruder | |
CN102303401B (en) | Method and equipment for simultaneously forming multiple high polymer thin bars by single screw machine barrel | |
CN202922922U (en) | Injection molding machine cylinder | |
CN103587025A (en) | Process for molding butadiene-component-containing plastic thin-wall product | |
CN102603983B (en) | Method for preparing polypropylene with high-melt-strength by modifying T30s through acetone solvent method | |
CN204773488U (en) | Novel special double screw extruder of polymer plastic | |
CN109849256A (en) | Instrument housing resin injection molding technique | |
US11325281B2 (en) | Rapid manufacturing of tailored preforms |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |