CN1059571A - Manufacturing is by the polymer particularly artificial long tow that forms of polyamide, polyester or polypropylene or the method and apparatus of artificial fibre - Google Patents
Manufacturing is by the polymer particularly artificial long tow that forms of polyamide, polyester or polypropylene or the method and apparatus of artificial fibre Download PDFInfo
- Publication number
- CN1059571A CN1059571A CN91104039A CN91104039A CN1059571A CN 1059571 A CN1059571 A CN 1059571A CN 91104039 A CN91104039 A CN 91104039A CN 91104039 A CN91104039 A CN 91104039A CN 1059571 A CN1059571 A CN 1059571A
- Authority
- CN
- China
- Prior art keywords
- filament
- micro
- thermal treatment
- mentioned
- artificial
- 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.)
- Granted
Links
Images
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/098—Melt spinning methods with simultaneous stretching
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/088—Cooling filaments, threads or the like, leaving the spinnerettes
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Textile Engineering (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
A kind of artificial long tow that forms by polymer or method of oriented yarn yarn entirely made, wherein, carry out the melt spinning of micro filament, these micro filaments are cooled to setting temperature at least after spinning head, and be heated to more than the freezing point temperature, so that stretch, simultaneously dash with air and blow above-mentioned long filament in order to produce required tensile stress.The filament fiber number is passed the thermal treatment zone less than the micro filament of 1.0 dtexs under the state of bunchy orientation not, and with air along countercurrent direction towards blowing.This artificial long tow has quite little percentage elongation, and can directly use, promptly according to the fineness of endless tow, no longer carry out post processing just can produce meticulous especially, submissive, as the silk textiles.
Description
The present invention relates to a kind of manufacturing by the polymer particularly artificial long tow that forms of polyamide, polyester or polypropylene or the method for artificial fibre, wherein in the melt spinning process of micro filament, at least be cooled to setting temperature in the cooling zone of micro filament after spinning head with the given speed drawing-off, then be heated on the freezing point temperature in the thermal treatment zone, so that stretch, in order to improve frictional resistance and to produce required tensile stress, blow to micro filament simultaneously with a kind of gaseous medium.
Such method is known: the artificial filament who promptly passes the thermal treatment zone is laterally dashed by air draught and blows.This artificial filament is by 50 long filaments or claim monofilament to form, and wherein long filament or filament number can be 1.0 dtexs where necessary, and general provision is 3.0 dtexs.The above-mentioned thermal treatment zone is made of a proportional heating tube of length, and its length is 3 meters.The long filament of being extracted out by spinning head has been formed the artificial long tow that will be heated in order to stretching after cooling and be integrated bundle before entering heating tube.The result of bunchy has caused the mutual applying between the long filament like this, has caused uneven heat treated thus.This is disadvantageous for various reasons.At first, drawing process will be affected, and be almost impossible because at this moment long filament is heated to more than the freezing point equably, be almost impossible so artificial long tow's entire cross section evenly is heated to more than the freezing point temperature.Artificial long tow's state relation is to the raising of frictional resistance, so that produce the required tensile stress that stretches.Here only dash in cross-sectional direction and blow this artificial long tow, this operation will be difficult.General draw rate or winding speed can not improve arbitrarily in above-mentioned known method, only are 3500 meters/minute.This is not only unfavorable to productivity ratio, and has the percentage elongation of proportional increase with the artificial long tow that this known method is produced, if the words of its filament fiber number>1.0 dtexs.This artificial long tow need carry out post processing just can be used for weaving processing.At last, because water back or heating path are longer, this artificial long tow's manufacturing equipment is built quite tall and big.
Therefore the purpose of this invention is to provide a kind of method, produce full stretching artificial long tow or artificial fibre (FOY=fully oriented filament) by this method with high production rate, these artificial long tows or artificial fibre do not need post processing just can be directly used in textile industry, and can be processed into meticulous especially, submissive or as the product of real silk.In addition, the present invention also provide a kind of corresponding, build very short and small equipment.
The method that provides according to an aspect of of the present present invention has solved above-mentioned task, i.e. the micro filament of filament fiber number<1.0 dtexs boundling orientation not, and just they pass the thermal treatment zone in parallel to each other, and are dashed along countercurrent direction by gaseous medium such as air and to blow.Adopting the filament fiber number in preferred version is the micro filament of 0.4 to 0.8 dtex.Technical scheme of the present invention builds on the following understanding basis: dash with adverse current and blow micro filament and can improve frictional resistance, and can form without difficulty and extend required tensile stress fully.Contrary air-flow means higher air drag, so the raising of draft speed increases the tension force of long filament.Leng Que micro filament was heated to its freezing point temperature again when above before reeling in the thermal treatment zone in the ban, and good stretching causes that the tension force of endless tow increases.According to technical scheme of the present invention, micro filament passes from the thermal treatment zone under the state of bunchy not, thereby the entire cross section of micro filament is all evenly heated.This even heating has promoted the full orientation or the stretching of micro filament, and then has also promoted corresponding artificial long tow's full orientation or stretching.Above-mentioned artificial long tow or all show low especially percentage elongation by its artificial fibre made or the staple fibre that is used for (weak point) silvalin.Because the fiber number of long filament is less, they need not carry out other post processings, just can use.Like this, with the inventive method make endless tow can make meticulous, submissive, as the product of real silk.The method according to this invention, the stretching of micro filament is only carried out in air drag and under the temperature of the thermal treatment zone.Therefore, as far as possible little fiber number particularly filament number is particularly advantageous, because like this can be comparatively fast and control easily or adjust the tension force and the temperature of long filament.In addition, still can produce with higher draft speed although shortened thermal treatment zone the present invention, thus the productivity ratio that improves.
The further inner characteristic of the present invention now is described below.The present invention stipulates like this: in contrary air-flow the temperature of heating micro filament between 150 ℃ to 250 ℃, preferred 220 ℃; The draft speed that these micro filaments pass the thermal treatment zone 3500 meters/assign between 8000 meters/minute preferred 4500 meters/assign to 5500 meters/minute.The micro filament of heating is gathered bunchy by rights after passing the thermal treatment zone and before reeling, thereby carries out handling especially uniformly and stretching in the thermal treatment zone.
Object of the present invention also relates to a kind of equipment, and this equipment is owing to simple and compact for structurely be very suitable for implementing said method.This equipment has a spinning head, a spinning shaft, a heating path, a pretreatment unit, a godet roller and a coiler device at least, it is characterized in that: described heating path has the air-blast device of the contrary air-flow of a generation in discharge one side, air-blast nozzle for example, this heating path is positioned at 0.8 meter to 1.2 meters, spinning head below, is provided with along the filament drawing direction.This heating path length is 1 meter to 1.5 meters, preferred 1.2 meters.Like this, compare with known equipment, the construction height of the thermal treatment zone is actual to have reduced 50%.In addition, micro filament and will change by the heating-up temperature in heating path and the change of counter-flow air quantity delivered by its artificial long tow's who produces degree of drawing.
Embodiment below with reference to accompanying drawings, the invention will be further described.
Unique accompanying drawing has been expressed the full orientation artificial long tow's 1 that manufacturing of the present invention is made of micro filament 2 equipment.The basic structure of this equipment comprises: a spinning head 3 that produces micro filament 2 is cooled in these micro filaments 2 spinning shaft 4 below.Below spinning shaft 4, be provided with a heating path 5, micro filament not have bundle together but with the state that is parallel to each other by above-mentioned heating path 5, this micro filament be heated and along the countercurrent direction quilt towards blowing.This countercurrent direction is represented with arrow.Is a pretreatment unit 6 in heating below the path 5, just lubricator or respective nozzles.On this pretreatment unit 6, micro filament 2 is integrated a branch of, becomes a branch of artificial long tow 1.Then, this artificial long tow 1 is directed into winding head through the godet roller 7 of coiler device 8, and reels.Above-mentioned heating path 5 is positioned at 0.8 meter to 1.2 meters, spinning head 3 belows, is provided with along the filament drawing direction.The length in heating path is 1 meter to 1.5 meters, and present embodiment is 1.2 meters.In addition, this heating path 5 has an air-blast device 9 that produces adverse current, for example is an air-blast nozzle.
Artificial long tow made according to the method for the present invention, its percentage elongation<40% is preferably 20% to 30%; Its intensity>3.6 are preferably>4 lis of newton (CN)/dtex).Process under 4500 meters/minute the condition if be at draft speed, and the filament number of micro filament<1.0 dtexs, perhaps artificial long tow's total fiber number is 30/48 dtex, and also promptly this artificial long tow is made of 48 micro filaments or monofilament, so just can obtain above-mentioned percentage elongation and strength values.Following table will make us very clear.
Draft speed rice/minute | 3500 | 4500 | 4500 |
The tensile strength path temperature ℃ preoriented yarn one percentage elongation % of endless tow fineness dtex percentage elongation % intensity li newton/dtex Wu Site N% |
83,7/48 48,48 3,6 0,99 32,5 185 108,4 | 85,3/48 42,75 3,79 0,87 41,0 125 74,8 | 30,6/48 27,65 4,11 1,58 38,5 188 66,9 |
Claims (7)
1, a kind of artificial long tow that is made up of polymer, particularly polyamide, polyester or polypropylene or method of artificial fibre made wherein carried out the melt spinning of micro filament; Then, be cooled to setting temperature at least in the cooling zone of micro filament after spinning head with the given speed drawing-off; Then, above-mentioned micro filament is heated to more than the freezing point temperature in the thermal treatment zone, so that stretch, dash with gaseous medium such as air simultaneously and blow above-mentioned micro filament, to improve frictional resistance or to produce required tensile stress, it is characterized in that: the micro filament of filament fiber number<1.0 dtexs passes the thermal treatment zone under the state of the orientation of bunchy not, and is dashed with countercurrent direction by gas medium and to blow.
2, in accordance with the method for claim 1, it is characterized in that: the filament fiber number of the micro filament of processed processing is 0.4 to 0.8 dtex.
3, according to claim 1 or 2 described methods, it is characterized in that: above-mentioned micro filament is heated to 150 ℃ to 250 ℃ in the thermal treatment zone in adverse current, preferred 220 ℃.
4, according to one of in the claim 1 to 3 method, it is characterized in that: above-mentioned micro filament is with 3500 meters/minute to 8000 meters/minute, and preferred 4500 meters/minute to 5500 meters/minute draft speed passes the thermal treatment zone.
5, according to one of in the claim 1 to 4 method, it is characterized in that: above-mentioned processed micro filament is the thermal treatment zone after and be integrated bundle before coiling.
6, implement the equipment of the method for one of claim 1 to 5, has at least one spinning head, a spinning shaft, a heating path, a pretreatment unit, a godet roller, a coiler device, it is characterized in that: above-mentioned heating path (5) has the air-blast device (9) that produces contrary air-flow in discharge one side, as air-blast nozzle.
7, according to the described equipment of claim 6, it is characterized in that: above-mentioned heating path (5) is positioned at 0.8 to 1.2 meter, above-mentioned spinning head (3) below, be provided with along the filament drawing direction, the length of path (5) between 1 to 1.5 meter, preferred 1.2 meters.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEP4021545.8 | 1990-07-06 | ||
DE4021545A DE4021545A1 (en) | 1990-07-06 | 1990-07-06 | METHOD AND DEVICE FOR PRODUCING PLASTIC FEATHERS OR FIBERS FROM POLYMERS, ESPECIALLY POLYAMIDE, POLYESTER OR POLYPROPYLENE |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1059571A true CN1059571A (en) | 1992-03-18 |
CN1050392C CN1050392C (en) | 2000-03-15 |
Family
ID=6409778
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN91104039A Expired - Fee Related CN1050392C (en) | 1990-07-06 | 1991-07-05 | Method and apparatus for manufacturing artificial filament or artificial fibre comprising polymers especially for polyamide, polyester or polypropylene |
Country Status (8)
Country | Link |
---|---|
EP (1) | EP0491012B1 (en) |
KR (1) | KR950001648B1 (en) |
CN (1) | CN1050392C (en) |
DE (2) | DE4021545A1 (en) |
ES (1) | ES2098354T3 (en) |
GR (1) | GR3022728T3 (en) |
ID (1) | ID17300A (en) |
WO (1) | WO1992001093A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1063497C (en) * | 1995-08-08 | 2001-03-21 | 克鲁普犹德有限公司 | Method and apparatus for producing polyester fibers |
CN102131965B (en) * | 2008-08-27 | 2012-09-05 | 欧瑞康纺织有限及两合公司 | Method for melt spinning, stretching and winding multifilament thread and device for carrying out same |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5318985A (en) * | 1991-12-20 | 1994-06-07 | Merrell Dow Pharmaceuticals Inc. | Potentiation of NMDA antagonists |
DE19705113C2 (en) * | 1997-02-12 | 1999-04-29 | Freudenberg Carl Fa | Stretching device and method for producing stretched plastic filaments |
DE19802086B4 (en) * | 1998-01-21 | 2007-02-15 | Uhde Gmbh | Method and device for producing plastic threads or staple fibers from polymers, in particular PET, CO-PET and / or PBT |
DE19816979A1 (en) * | 1998-04-17 | 1999-10-21 | Brown John Deutsche Eng Gmbh | Method and device for producing polyester yarns |
DE19821778B4 (en) * | 1998-05-14 | 2004-05-06 | Ems-Inventa Ag | Device and method for producing microfilaments of high titer uniformity from thermoplastic polymers |
DE10139228A1 (en) * | 2001-08-09 | 2003-03-06 | Freudenberg Carl Kg | Stretching device and method for producing stretched plastic filaments |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2117659A1 (en) * | 1971-04-10 | 1972-10-19 | Farbwerke Hoechst AG, vormals Meister Lucius & Brüning, 6000 Frankfurt | Process for making threads and fibers |
US3946100A (en) * | 1973-09-26 | 1976-03-23 | Celanese Corporation | Process for the expeditious formation and structural modification of polyester fibers |
DE2925006C2 (en) * | 1979-06-21 | 1983-06-30 | Akzo Gmbh, 5600 Wuppertal | Process for the production of melt-spun and molecularly oriented drawn, crystalline filaments |
EP0034880B1 (en) * | 1980-02-18 | 1986-03-05 | Imperial Chemical Industries Plc | Process for forming a continuous filament yarn from a melt spinnable polyethylene terephthalat and novel polyester yarns produced by the process |
EP0042664B1 (en) * | 1980-06-24 | 1983-09-21 | Imperial Chemical Industries Plc | Polyester yarns produced by high speed melt-spinning processes |
CA1233009A (en) * | 1983-09-14 | 1988-02-23 | Cornell Whitley | High speed process for forming fully drawn polyester yarn |
-
1990
- 1990-07-06 DE DE4021545A patent/DE4021545A1/en active Granted
-
1991
- 1991-05-18 WO PCT/DE1991/000420 patent/WO1992001093A1/en active IP Right Grant
- 1991-05-18 EP EP91909385A patent/EP0491012B1/en not_active Expired - Lifetime
- 1991-05-18 ES ES91909385T patent/ES2098354T3/en not_active Expired - Lifetime
- 1991-05-18 KR KR1019920700491A patent/KR950001648B1/en not_active IP Right Cessation
- 1991-05-18 DE DE59108570T patent/DE59108570D1/en not_active Expired - Fee Related
- 1991-07-05 CN CN91104039A patent/CN1050392C/en not_active Expired - Fee Related
- 1991-11-04 ID IDP83991A patent/ID17300A/en unknown
-
1997
- 1997-03-03 GR GR970400419T patent/GR3022728T3/en unknown
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1063497C (en) * | 1995-08-08 | 2001-03-21 | 克鲁普犹德有限公司 | Method and apparatus for producing polyester fibers |
CN102131965B (en) * | 2008-08-27 | 2012-09-05 | 欧瑞康纺织有限及两合公司 | Method for melt spinning, stretching and winding multifilament thread and device for carrying out same |
Also Published As
Publication number | Publication date |
---|---|
DE4021545C2 (en) | 1992-07-09 |
ID17300A (en) | 1997-12-18 |
WO1992001093A1 (en) | 1992-01-23 |
EP0491012B1 (en) | 1997-02-26 |
KR920702446A (en) | 1992-09-04 |
ES2098354T3 (en) | 1997-05-01 |
GR3022728T3 (en) | 1997-06-30 |
KR950001648B1 (en) | 1995-02-27 |
DE4021545A1 (en) | 1992-01-16 |
DE59108570D1 (en) | 1997-04-03 |
EP0491012A1 (en) | 1992-06-24 |
CN1050392C (en) | 2000-03-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN1046321C (en) | Method and apparatus for producing polyester fiber | |
TWI494477B (en) | Method for drawing-off and stretching a multifilament thread during melt-spinning as well as a device for performing the method | |
CN102131965B (en) | Method for melt spinning, stretching and winding multifilament thread and device for carrying out same | |
EP2456912A1 (en) | Method for removing and drawing a synthetic thread and a device for performing the method | |
US2957747A (en) | Process for producing crimpable polyamide filaments | |
US6635199B2 (en) | Process for producing a precursor fiber bundle and a carbon fiber bundle | |
US4035464A (en) | Process for the production of polyamide-6 filament yarns | |
US6210622B1 (en) | Process of making polymeric fibers | |
CN1050392C (en) | Method and apparatus for manufacturing artificial filament or artificial fibre comprising polymers especially for polyamide, polyester or polypropylene | |
CN1142334C (en) | Method for texturing synthetic filament false twist crimping into crimped filament | |
CN1328423C (en) | Method for producing highly stable polypropylene fibres | |
DE102009037125A1 (en) | Method for melt-spinning, drawing and winding multifilament thread during manufacture of synthetic fiber for textile applications, involves guiding bundle at specific drawing speed, and winding yarn into spool | |
CN100379914C (en) | Oven for drawing fibres at elevated temp | |
JPH04228605A (en) | Spinning apparatus of synthetic molten fiber-forming polymer | |
KR100267601B1 (en) | Process and device for producing polyester yarns | |
CN106795652A (en) | Method and apparatus for producing multifilament threads by polyamide melt | |
CN107109704A (en) | Method and apparatus for producing multifilament yarn | |
RU2318930C2 (en) | Spinning method | |
KR20100033246A (en) | Spining machine having a heating/cooling setting system | |
US5277859A (en) | Method for the production of polypropylene yarn | |
KR102263320B1 (en) | Monofilament Yarn Manufacturing System and Method | |
US5538792A (en) | Process for drawing heated yarns, thereby obtainable polyester fibers, and use thereof | |
JPH04228612A (en) | High tension, high initial modulus and low shrink properties drawing polyester thread | |
JPH09228138A (en) | Production of thermoplastic fiber and apparatus therefor | |
CA1152273A (en) | Process for forming a continuous filament yarn from a melt spinnable synthetic polymer and novel polyester yarns produced by the process |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C53 | Correction of patent for invention or patent application | ||
COR | Change of bibliographic data |
Free format text: CORRECT: PATENTEE; FROM: FIRTH, GERMANY - APING INDUSTRIAL CONSTRUCTION PROJECT CONSULTING CO., LTD. TO: KRUPP UHDE GMBH |
|
CP03 | Change of name, title or address |
Address after: Dortmund, Germany Patentee after: Krupp Uhde GMBH Address before: Essen, Germany Patentee before: Der Voest-Alpine Industrieanlagenbau GMBH |
|
C15 | Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993) | ||
OR01 | Other related matters | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |