EP0970269B1 - Verfahren zur herstellung von monofilamenten aus polyamid und monofilament für technische gewebe - Google Patents
Verfahren zur herstellung von monofilamenten aus polyamid und monofilament für technische gewebe Download PDFInfo
- Publication number
- EP0970269B1 EP0970269B1 EP98906784A EP98906784A EP0970269B1 EP 0970269 B1 EP0970269 B1 EP 0970269B1 EP 98906784 A EP98906784 A EP 98906784A EP 98906784 A EP98906784 A EP 98906784A EP 0970269 B1 EP0970269 B1 EP 0970269B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- monofilament
- process according
- diameter
- monofilaments
- mixture
- 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
- 239000004744 fabric Substances 0.000 title claims description 11
- 239000004952 Polyamide Substances 0.000 title claims description 5
- 229920002647 polyamide Polymers 0.000 title claims description 5
- 238000004519 manufacturing process Methods 0.000 title description 9
- 229920002292 Nylon 6 Polymers 0.000 claims description 16
- 229920002302 Nylon 6,6 Polymers 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 10
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000001125 extrusion Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 2
- 238000009987 spinning Methods 0.000 claims description 2
- 239000008188 pellet Substances 0.000 claims 2
- 206010003549 asthenia Diseases 0.000 claims 1
- 239000007787 solid Substances 0.000 description 8
- 239000008187 granular material Substances 0.000 description 6
- 229920000642 polymer Polymers 0.000 description 5
- 210000003934 vacuole Anatomy 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000010949 copper Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 150000001879 copper Chemical class 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000002787 reinforcement Effects 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 description 1
- 229910021590 Copper(II) bromide Inorganic materials 0.000 description 1
- 229910021592 Copper(II) chloride Inorganic materials 0.000 description 1
- VCUFZILGIRCDQQ-KRWDZBQOSA-N N-[[(5S)-2-oxo-3-(2-oxo-3H-1,3-benzoxazol-6-yl)-1,3-oxazolidin-5-yl]methyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C1O[C@H](CN1C1=CC2=C(NC(O2)=O)C=C1)CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F VCUFZILGIRCDQQ-KRWDZBQOSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000003490 calendering Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- QTMDXZNDVAMKGV-UHFFFAOYSA-L copper(II) bromide Substances [Cu+2].[Br-].[Br-] QTMDXZNDVAMKGV-UHFFFAOYSA-L 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
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
- D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
- D01F6/90—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyamides
Definitions
- the invention relates to a method for producing vacuole-free, heat-protected, round monofilaments made of polyamide for technical fabrics.
- the object of the invention is to provide a method to ask with which vacuole coarse monofilaments made of light synthetic material for use in fabrics for Carcasses or other textile insert materials in heavy tires can be produced.
- the object is achieved by solved a process for producing the monofilaments, where the monofilaments are made from a mixture of 75-85% by weight of PA 66 and 15 up to 25 wt .-% PA 6 and the mixture immediately before extruding mixed, spun and directly in a liquid is cooled.
- the addition of all the heat protection, embedded in the PA-66 polymer granulate has the advantage of good final mixing in the monofilament without any noteworthy Degradation of the polymer and the copper is caused by the Embedding in the polymer prevented, for example on Extruder tube to be sintered.
- the copper is in the form of a Copper salt used. When copper salt comes preferably a halide such as copper (II) chloride, bromide or iodide in question.
- PA 66 and PA 6 in Granulate form an extruder, especially one Add degassing extruder.
- a grain weight of less than 10 mg leads to the most common Feed augers for feeding problems; a grain weight of more than 100 mg leads to a bad one Mixing. It is important to ensure that the Grain size of the granules for PA 66 and PA 6 approximately the same is.
- a monofilament for technical fabrics with a round one Cross section from 0.8 to 1.5 mm, preferably 0.9 to 1.2 mm and a melting point range of 235-260 ° C is preferred 245 ° C-260 ° C, especially 255 - 260 ° C is especially for Manufacture of fabrics for use in carcasses and Suitable for breakers in tires.
- Has a round cross section the advantage over a non-round cross-section, that the monofilament is processing calendered fabrics not twisted.
- a monofilament thickness of ⁇ 0.8 mm has the disadvantages of an insufficient Tear resistance and stability; a monofilament thickness of> 1.5 can no longer be manufactured.
- Loss of tensile strength 7-day heat treatment at 190 ° C.
- PA 6 solid Polyamide 6
- PA 66 solid polyamide 66
- the PA 66 contains 100 ppm Cu as Heat protection.
- the mixed polymer granules, with a Grain weight from 14 to 64 mg, is in one Twin screw extruder melted using vacuum moisture is removed from the melt and then carried out.
- the polymer melt is over a vertically arranged spinning head in a water bath extruded.
- the diameter of the multi-hole round hole nozzle is 3.4 mm and the extrusion speed is 12.8 m / min.
- the raw wire is in a water bath, with a distance of 80 mm to the nozzle plate and a temperature of 40 ° C cooled.
- the monofilament is still hot inside withdrawn from the cooling bath via two delivery rolls and over another cooling section, with a water temperature of 15-20 ° C, fed to a stretching process.
- the stretching of the monofilament is made in a ratio of 1: 4 to 5 subsequent relaxation.
- the monofilament according to the invention is particularly suitable for Manufacture of tire reinforcement fabrics and there in Chain insert, but also for paper machine screens in Wet area, as well as suitable for fishing.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Artificial Filaments (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH66997 | 1997-03-20 | ||
CH66997 | 1997-03-20 | ||
PCT/CH1998/000100 WO1998042900A1 (de) | 1997-03-20 | 1998-03-16 | Verfahren zur herstellung von monofilamenten aus polyamid und monofilament für technische gewebe |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0970269A1 EP0970269A1 (de) | 2000-01-12 |
EP0970269B1 true EP0970269B1 (de) | 2002-09-11 |
Family
ID=4192397
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP98906784A Expired - Lifetime EP0970269B1 (de) | 1997-03-20 | 1998-03-16 | Verfahren zur herstellung von monofilamenten aus polyamid und monofilament für technische gewebe |
Country Status (13)
Country | Link |
---|---|
US (1) | US6238608B1 (id) |
EP (1) | EP0970269B1 (id) |
JP (1) | JP2001518152A (id) |
KR (1) | KR20000076341A (id) |
AR (1) | AR011096A1 (id) |
AT (1) | ATE223981T1 (id) |
BR (1) | BR9808286A (id) |
DE (1) | DE59805514D1 (id) |
DK (1) | DK0970269T3 (id) |
EA (1) | EA000984B1 (id) |
ID (1) | ID22387A (id) |
PT (1) | PT970269E (id) |
WO (1) | WO1998042900A1 (id) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080132636A1 (en) * | 2004-06-03 | 2008-06-05 | Gilbert Ross | Nylon monofilaments and process for preparing nylon monofilaments for the production of spiral fabrics and seam wires |
US20060033231A1 (en) * | 2004-08-10 | 2006-02-16 | Reuter Rene F | Monofilament reinforced rubber component and method of producing |
US20080182938A1 (en) * | 2007-01-25 | 2008-07-31 | Heping Zhang | Toughened monofilaments |
EP2597179B1 (de) * | 2011-11-24 | 2014-01-08 | EMS-Patent AG | Flammhemmende Polymerfasern und deren Verwendung sowie diese Polymerfasern enthaltendes Textilgewebe |
CN109706565A (zh) * | 2019-02-18 | 2019-05-03 | 海安县中祥线业有限公司 | 多公斤级无结线制备工艺 |
CN114957988A (zh) * | 2022-07-14 | 2022-08-30 | 四川朗迪新材料有限公司 | 一种阻燃玻纤增强pa66/pp合金组合物 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
ZA71465B (en) * | 1970-02-17 | 1971-10-27 | Du Pont | Colorless polyamide compositions and shaped articles stabilized for weatherability |
JPS59157314A (ja) * | 1983-02-18 | 1984-09-06 | Mitsubishi Chem Ind Ltd | ポリアミドモノフイラメントの製造法 |
DE3601565A1 (de) * | 1986-01-21 | 1987-07-23 | Bayer Ag | Verfahren zur herstellung von spiralsieben |
US5262099A (en) | 1992-04-01 | 1993-11-16 | E. I. Du Pont De Nemours And Company | Process of making high tenacity polyamide monofilaments |
JP3234295B2 (ja) * | 1992-08-27 | 2001-12-04 | 旭化成株式会社 | ポリヘキサメチレンアジパミド繊維の製造方法 |
JPH0881823A (ja) * | 1994-09-08 | 1996-03-26 | Toray Monofilament Co Ltd | 延縄用ポリアミドモノフィラメントおよびその製造方法 |
-
1998
- 1998-01-29 AR ARP980100395A patent/AR011096A1/es unknown
- 1998-03-16 EA EA199900852A patent/EA000984B1/ru not_active IP Right Cessation
- 1998-03-16 PT PT98906784T patent/PT970269E/pt unknown
- 1998-03-16 BR BR9808286-8A patent/BR9808286A/pt active Search and Examination
- 1998-03-16 KR KR1019997008442A patent/KR20000076341A/ko active IP Right Grant
- 1998-03-16 AT AT98906784T patent/ATE223981T1/de not_active IP Right Cessation
- 1998-03-16 JP JP54462198A patent/JP2001518152A/ja not_active Abandoned
- 1998-03-16 WO PCT/CH1998/000100 patent/WO1998042900A1/de active IP Right Grant
- 1998-03-16 DE DE59805514T patent/DE59805514D1/de not_active Expired - Fee Related
- 1998-03-16 US US09/380,451 patent/US6238608B1/en not_active Expired - Fee Related
- 1998-03-16 DK DK98906784T patent/DK0970269T3/da active
- 1998-03-16 EP EP98906784A patent/EP0970269B1/de not_active Expired - Lifetime
-
1999
- 1999-03-16 ID IDW991039A patent/ID22387A/id unknown
Also Published As
Publication number | Publication date |
---|---|
ATE223981T1 (de) | 2002-09-15 |
US6238608B1 (en) | 2001-05-29 |
DK0970269T3 (da) | 2003-09-08 |
WO1998042900A1 (de) | 1998-10-01 |
BR9808286A (pt) | 2000-05-16 |
EA199900852A1 (ru) | 2000-04-24 |
PT970269E (pt) | 2003-03-31 |
ID22387A (id) | 1999-10-07 |
EA000984B1 (ru) | 2000-08-28 |
DE59805514D1 (de) | 2002-10-17 |
JP2001518152A (ja) | 2001-10-09 |
EP0970269A1 (de) | 2000-01-12 |
AR011096A1 (es) | 2000-08-02 |
KR20000076341A (ko) | 2000-12-26 |
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