CN104831381A - Production method of glazed extra-black trefoil polyester FDY (Fully Drawn Yarn) - Google Patents

Production method of glazed extra-black trefoil polyester FDY (Fully Drawn Yarn) Download PDF

Info

Publication number
CN104831381A
CN104831381A CN201510206644.0A CN201510206644A CN104831381A CN 104831381 A CN104831381 A CN 104831381A CN 201510206644 A CN201510206644 A CN 201510206644A CN 104831381 A CN104831381 A CN 104831381A
Authority
CN
China
Prior art keywords
pet
black
district
production method
temperature
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
Application number
CN201510206644.0A
Other languages
Chinese (zh)
Inventor
翁建男
王超
罗峰
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.)
Suzhou Is As Contained Chemical Fibre Co Ltd
Original Assignee
Suzhou Is As Contained Chemical Fibre 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 Suzhou Is As Contained Chemical Fibre Co Ltd filed Critical Suzhou Is As Contained Chemical Fibre Co Ltd
Priority to CN201510206644.0A priority Critical patent/CN104831381A/en
Publication of CN104831381A publication Critical patent/CN104831381A/en
Pending legal-status Critical Current

Links

Abstract

The invention relates to a production method of a glazed extra-black trefoil polyester FDY (Fully Drawn Yarn). The production method comprises the following steps: (a) weighing 92% to 94% of glazed PET chips (polyester chips) for pre-crystallization and drying in weight, and weighing 6% to 8% of black master batch for drying in weight; (b) manufacturing the dried glazed PET chips and the dried black master batch after being mixed into PET melts through a screw extruder; (c) filtering and pressing the PET melts and then distributing the filtered and pressed PET melts to each spinning assembly through a metering pump to generate nascent fibers, and adopting trefoil profiled spinneret plates; (d) winding and forming the nascent fibers after side air blowing cooling, lubricating nipple oiling, stretching shaping and gridding adding. On one hand, the glazed PET chips and the black master batch are mixed to manufacture the PET melts, so that the PET melts can be used for preparing the glazed extra-black trefoil polyester FDY; on the other hand, the spinning assemblies adopt the trefoil profiled spinneret plates, the included angle between the blades of the spinneret plates is 120 degrees, the blade length-width ratio is 5 to 10: 1, and thus the trefoil profiled FDY is formed.

Description

A kind of production method having the goth black three leaf polyester FDY long filaments of light
Technical field
The invention belongs to polymeric material field, relate to a kind of polyester FDY long filament, be specifically related to a kind of production method having the goth black three leaf polyester FDY long filaments of light.
Background technology
Dacron and people live closely bound up, are closely connected, for drapery, bedding, adornment, case and bag articles for use, tent etc.Polyester FDY (full name Fully Drawn Yarn, fullly drawn yarn (FDY)) introduces stretching action in spinning process, can obtain the undrawn yarn with high-orientation and crystalline medium degree.The smooth softness of polyester FDY fabric feel, is often used in and weaves silk-like fabric.Existing white polyester FDY filament can not meet daily life demand to a certain extent, therefore needs to make improvements.Goth black FDY filament is a kind of special modified fiber, and this kind adds black agglomerate on the basis of the white silk of former FDY, forms, can save dyeing link through certain processes.Meanwhile, the productive rate in chemical fibre market sharply rises, and causes the dacron product situation that supply exceed demand to become increasingly conspicuous, and adds national more and more higher to the requirement of environmental protection, is necessary to develop goth black FDY filament that is differential, functionalization.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of production method having the goth black three leaf polyester FDY long filaments of light.
For achieving the above object, the technical solution used in the present invention is: a kind of production method having the goth black three leaf polyester FDY long filaments of light, and it comprises the following steps:
(a) by weight, take 92% ~ 94% have light PET cut into slices pre-crystallized, dry; By weight, 6% ~ 8% black agglomerate is taken dry;
B () has light PET to cut into slices by dried and make PET melt through screw extruder after the mixing of dried black agglomerate;
C () produces as-spun fibre by being assigned to each spinning pack through measuring pump after described PET melt filter-press, the pressure of described spinning pack is 18 ~ 20MPa, it adopts three leaf profile spinnerets, and the angle between described spinnerets blade is 120 °, and described spinnerets blade length-width ratio is 5 ~ 10:1;
(d) by described as-spun fibre through lateral blowing cooling, oil nozzle oils, set-stretching, add coiling and molding after grid.
Optimally, in step (a), described in have light PET pre-crystallized temperature of cutting into slices to be 165 ~ 170 DEG C, baking temperature is 170 ~ 175 DEG C, and dry air pressure is 0.18 ~ 0.22MPa, and dry air dew point controls below-80 DEG C; The baking temperature of described black agglomerate is 130 ~ 150 DEG C.
Optimally, in step (b), screw rod each district temperature of described screw extruder is: 250 ~ 255 DEG C, a district, 260 ~ 265 DEG C, 2nd district, 265 ~ 270 DEG C, 3rd district, 275 ~ 280 DEG C, 4th district, 280 ~ 283 DEG C, 5th district, 285 ~ 288 DEG C, 6th district, and the temperature of described PET melt is 285 ~ 288 DEG C.
Optimally, in described step (d), lateral blowing temperature is 20 ~ 25 DEG C, and its flow direction parallels with one of them blade of described spinnerets, and air conditioning exhausting blast 400 ~ 600Pa, the blast entering ring blow head is 25 ~ 30Pa, and humidity is 70 ~ 80%.
Optimally, in described step (d), the first hot-rolling speed is 1500 ~ 2000m/min, and temperature is 80 ~ 90 DEG C; Second hot-rolling speed is 4000 ~ 4500m/min, and temperature is 120 ~ 130 DEG C; Winding speed is 4000 ~ 4500m/min, and Winding Tension Controlling is 10 ~ 15 li of oxen.
Because technique scheme is used, the present invention compared with prior art has following advantages: the present invention has the production method of the goth black three leaf polyester FDY long filaments of light, light PET being had on the one hand to cut into slices and make PET melt after black agglomerate mixing, making it possible to for the preparation of there being the goth black polyester FDY long filament of light; Spinning pack adopts three leaf profile spinnerets on the other hand, and the angle between this spinnerets blade is 120 °, and blade length-width ratio is 5 ~ 10:1, thus forms three leaf abnormity FDY filament.
Detailed description of the invention
To be described in detail to the preferred embodiment of the invention below:
Embodiment 1
The present embodiment provides a kind of production method having the goth black three leaf polyester FDY long filaments of light, and it comprises the following steps:
(a) by weight, take 92% have light PET cut into slices (inherent viscosity 0.648dl/g, fusing point 260 DEG C, Yizheng Chemical Fiber Co., Ltd., SINOPEC) 165 DEG C pre-crystallized, 170 DEG C of dryings (dry air pressure is 0.18MPa, and dew point is-80 DEG C); By weight, take 8% black agglomerate (composition of raw materials of black agglomerate comprise 0.3 part of odium stearate, 5 parts of ultra-fine carbon blacks, 1 part of antioxidant 1010,10 parts of PE wax, 0.01 part of dihydroxy benaophenonel, 20 parts have light PET to cut into slices) 130 DEG C of dryings;
B () has light PET to cut into slices by dried and make PET melt through screw extruder after the mixing of dried black agglomerate, screw rod each district temperature of screw extruder is: 250 DEG C, a district, 260 DEG C, 2nd district, 265 DEG C, 3rd district, 275 DEG C, 4th district, 280 DEG C, 5th district, 285 DEG C, 6th district, makes the PET melt of 285 DEG C;
C () produces as-spun fibre by being assigned to each spinning pack through measuring pump after described PET melt filter-press, the pressure of spinning pack is 18MPa, and it adopts three leaf profile spinnerets, and the angle between spinnerets blade is 120 °, and its blade length-width ratio is 5:1;
D () through lateral blowing cooling, (lateral blowing temperature is 20 DEG C by described as-spun fibre, its flow direction parallels with one of them blade of spinnerets, air conditioning exhausting blast 400Pa, the blast entering ring blow head is 25Pa, humidity is 70%), oil nozzle oils, set-stretching (adopts two hot-rollings to stretch, first hot-rolling speed is 1500m/min, and temperature is 80 DEG C; Second hot-rolling speed is 4000m/min, and temperature is 120 DEG C), coiling and molding (winding speed of take up roll is 4000m/min, and Winding Tension Controlling is 10cN) after adding grid.
Embodiment 2
The present embodiment provides a kind of production method having the goth black three leaf polyester FDY long filaments of light, and it comprises the following steps:
(a) by weight, take 94% have light PET cut into slices (inherent viscosity 0.648dl/g, fusing point 260 DEG C, Yizheng Chemical Fiber Co., Ltd., SINOPEC) 170 DEG C pre-crystallized, 175 DEG C of dryings (dry air pressure is 0.22MPa, and dew point is-85 DEG C); By weight, take 6% black agglomerate (composition of raw materials of black agglomerate comprise 0.3 part of odium stearate, 5 parts of ultra-fine carbon blacks, 1 part of antioxidant 1010,10 parts of PE wax, 0.01 part of dihydroxy benaophenonel, 20 parts have light PET to cut into slices) 150 DEG C of dryings;
B () has light PET to cut into slices by dried and make PET melt through screw extruder after the mixing of dried black agglomerate, screw rod each district temperature of screw extruder is: 255 DEG C, a district, 265 DEG C, 2nd district, 270 DEG C, 3rd district, 280 DEG C, 4th district, 283 DEG C, 5th district, 288 DEG C, 6th district, makes the PET melt of 288 DEG C;
C () produces as-spun fibre by being assigned to each spinning pack through measuring pump after described PET melt filter-press, the pressure of spinning pack is 20MPa, and it adopts three leaf profile spinnerets, and the angle between spinnerets blade is 120 °, and its blade length-width ratio is 10:1;
D () through lateral blowing cooling, (lateral blowing temperature is 25 DEG C by described as-spun fibre, its flow direction parallels with one of them blade of spinnerets, air conditioning exhausting blast 600Pa, the blast entering ring blow head is 30Pa, humidity is 80%), oil nozzle oils, set-stretching (adopts two hot-rollings to stretch, first hot-rolling speed is 2500m/min, and temperature is 90 DEG C; Second hot-rolling speed is 4500m/min, and temperature is 130 DEG C), coiling and molding (winding speed of take up roll is 4500m/min, and Winding Tension Controlling is 15cN) after adding grid.
Embodiment 3
The present embodiment provides a kind of production method having the goth black three leaf polyester FDY long filaments of light, and it comprises the following steps:
(a) by weight, take 93% have light PET cut into slices (inherent viscosity 0.648dl/g, fusing point 260 DEG C, Yizheng Chemical Fiber Co., Ltd., SINOPEC) 168 DEG C pre-crystallized, 172 DEG C of dryings (dry air pressure is 0.20MPa, and dew point is-82 DEG C); By weight, take 6% black agglomerate (composition of raw materials of black agglomerate comprise 0.3 part of odium stearate, 5 parts of ultra-fine carbon blacks, 1 part of antioxidant 1010,10 parts of PE wax, 0.01 part of dihydroxy benaophenonel, 20 parts have light PET to cut into slices) 135 DEG C of dryings;
B () has light PET to cut into slices by dried and make PET melt through screw extruder after the mixing of dried black agglomerate, screw rod each district temperature of screw extruder is: 252 DEG C, a district, 262 DEG C, 2nd district, 268 DEG C, 3rd district, 278 DEG C, 4th district, 280 DEG C, 5th district, 285 DEG C, 6th district, makes the PET melt of 285 DEG C;
C () produces as-spun fibre by being assigned to each spinning pack through measuring pump after described PET melt filter-press, the pressure of spinning pack is 19MPa, and it adopts three leaf profile spinnerets, and the angle between spinnerets blade is 120 °, and its blade length-width ratio is 8:1;
D () through lateral blowing cooling, (lateral blowing temperature is 23 DEG C by described as-spun fibre, its flow direction parallels with one of them blade of spinnerets, air conditioning exhausting blast 450Pa, the blast entering ring blow head is 29Pa, humidity is 75%), oil nozzle oils, set-stretching (adopts two hot-rollings to stretch, first hot-rolling speed is 2200m/min, and temperature is 85 DEG C; Second hot-rolling speed is 4200m/min, and temperature is 125 DEG C), coiling and molding (winding speed of take up roll is 4200m/min, and Winding Tension Controlling is 12cN) after adding grid.
Above-described embodiment is only for illustrating technical conceive of the present invention and feature; its object is to person skilled in the art can be understood content of the present invention and implement according to this; can not limit the scope of the invention with this; all equivalences done according to Spirit Essence of the present invention change or modify, and all should be encompassed within protection scope of the present invention.

Claims (5)

1. have a production method for the goth black three leaf polyester FDY long filaments of light, it is characterized in that, it comprises the following steps:
(a) by weight, take 92% ~ 94% have light PET cut into slices pre-crystallized, dry; By weight, 6% ~ 8% black agglomerate is taken dry;
B () has light PET to cut into slices by dried and make PET melt through screw extruder after the mixing of dried black agglomerate;
C () produces as-spun fibre by being assigned to each spinning pack through measuring pump after described PET melt filter-press, the pressure of described spinning pack is 18 ~ 20MPa, it adopts three leaf profile spinnerets, and the angle between described spinnerets blade is 120 °, and described spinnerets blade length-width ratio is 5 ~ 10:1;
(d) by described as-spun fibre through lateral blowing cooling, oil nozzle oils, set-stretching, add coiling and molding after grid.
2. there is the production method of the goth black three leaf polyester FDY long filaments of light according to claim 1, it is characterized in that: in step (a), described have light PET pre-crystallized temperature of cutting into slices to be 165 ~ 170 DEG C, baking temperature is 170 ~ 175 DEG C, dry air pressure is 0.18 ~ 0.22MPa, and dry air dew point controls below-80 DEG C; The baking temperature of described black agglomerate is 130 ~ 150 DEG C.
3. there is the production method of the goth black three leaf polyester FDY long filaments of light according to claim 1, it is characterized in that: in step (b), screw rod each district temperature of described screw extruder is: 250 ~ 255 DEG C, a district, 260 ~ 265 DEG C, 2nd district, 265 ~ 270 DEG C, 3rd district, 275 ~ 280 DEG C, 4th district, 280 ~ 283 DEG C, 5th district, 285 ~ 288 DEG C, 6th district, and the temperature of described PET melt is 285 ~ 288 DEG C.
4. there is the production method of the goth black three leaf polyester FDY long filaments of light according to claim 1, it is characterized in that: in described step (d), lateral blowing temperature is 20 ~ 25 DEG C, its flow direction parallels with one of them blade of described spinnerets, air conditioning exhausting blast 400 ~ 600Pa, the blast entering ring blow head is 25 ~ 30Pa, and humidity is 70 ~ 80%.
5. have the production method of the goth black three leaf polyester FDY long filaments of light according to claim 1, it is characterized in that: in described step (d), the first hot-rolling speed is 1500 ~ 2000m/min, and temperature is 80 ~ 90 DEG C; Second hot-rolling speed is 4000 ~ 4500m/min, and temperature is 120 ~ 130 DEG C; Winding speed is 4000 ~ 4500m/min, and Winding Tension Controlling is 10 ~ 15 li of oxen.
CN201510206644.0A 2015-04-28 2015-04-28 Production method of glazed extra-black trefoil polyester FDY (Fully Drawn Yarn) Pending CN104831381A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510206644.0A CN104831381A (en) 2015-04-28 2015-04-28 Production method of glazed extra-black trefoil polyester FDY (Fully Drawn Yarn)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510206644.0A CN104831381A (en) 2015-04-28 2015-04-28 Production method of glazed extra-black trefoil polyester FDY (Fully Drawn Yarn)

Publications (1)

Publication Number Publication Date
CN104831381A true CN104831381A (en) 2015-08-12

Family

ID=53809565

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510206644.0A Pending CN104831381A (en) 2015-04-28 2015-04-28 Production method of glazed extra-black trefoil polyester FDY (Fully Drawn Yarn)

Country Status (1)

Country Link
CN (1) CN104831381A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107338500A (en) * 2016-09-28 2017-11-10 桐乡守敬应用技术研究院有限公司 A kind of production method of fine denier lustrous flame-resistant terylene FDY filament
CN108707985A (en) * 2018-08-09 2018-10-26 福建经纬新纤科技实业有限公司 A kind of polyester filament and preparation method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61275416A (en) * 1984-11-21 1986-12-05 Mitsubishi Rayon Co Ltd Acrylic yarn with y section and production thereof
CN1558003A (en) * 2004-01-16 2004-12-29 张志明 Terylene colored glossy profile monofilament and special purpose spinnerette for manufacturing the same
CN201801641U (en) * 2010-09-13 2011-04-20 浙江安顺化纤有限公司 Black brightening recycled polyester short fiber
CN102532666A (en) * 2012-01-05 2012-07-04 东莞市德诚塑化科技有限公司 Insulated black masterbatch and preparation method thereof
CN104532387A (en) * 2014-12-29 2015-04-22 张志明 Low-melting-point colored special-shaped polyester filament and preparation method thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61275416A (en) * 1984-11-21 1986-12-05 Mitsubishi Rayon Co Ltd Acrylic yarn with y section and production thereof
CN1558003A (en) * 2004-01-16 2004-12-29 张志明 Terylene colored glossy profile monofilament and special purpose spinnerette for manufacturing the same
CN201801641U (en) * 2010-09-13 2011-04-20 浙江安顺化纤有限公司 Black brightening recycled polyester short fiber
CN102532666A (en) * 2012-01-05 2012-07-04 东莞市德诚塑化科技有限公司 Insulated black masterbatch and preparation method thereof
CN104532387A (en) * 2014-12-29 2015-04-22 张志明 Low-melting-point colored special-shaped polyester filament and preparation method thereof

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
吴建亭: "母粒注射法生产三叶形黑色涤纶FDY", 《聚酯工业》 *
吴建亭: "黑色涤纶细旦FDY的生产工艺初探", 《合成纤维工业》 *
尹翠玉等: "三叶有色涤纶FDY生产工艺研究", 《纺织学报》 *
王永生: "母粒注射法生产黑色三叶形涤纶FDY", 《合成纤维工业》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107338500A (en) * 2016-09-28 2017-11-10 桐乡守敬应用技术研究院有限公司 A kind of production method of fine denier lustrous flame-resistant terylene FDY filament
CN108707985A (en) * 2018-08-09 2018-10-26 福建经纬新纤科技实业有限公司 A kind of polyester filament and preparation method thereof
CN108707985B (en) * 2018-08-09 2023-08-11 福建经纬新纤科技实业有限公司 Polyester filament yarn and preparation method thereof

Similar Documents

Publication Publication Date Title
CN104831403A (en) Three-blade irregular cationic terylene FDY filament and production method thereof
CN101956240B (en) Method for producing terylen fibers from polyester waste
CN103590139B (en) A kind of powerful three-dimensional crimp memory fiber and manufacture method thereof
CN102586939A (en) Profiled fire-retardant bright terylene FDY (Fully Drawn Yarn) filament and production process thereof
CN101225555B (en) Melt-spinning hot-stretch forming preparation method of polyetheretherketone fibre
CN111593422B (en) PETG (polyethylene terephthalate glycol) -based rapid-forming wig fiber and preparation process thereof
CN102409419B (en) Flexible and heterogeneous nylon-6 fiber
CN101532182B (en) polyester FDY filament with diamond luster and preparation process thereof
CN104727015A (en) Manufacturing method for melt-blown nonwoven fabric
CN104178844A (en) Aromatic chinlon-spandex air wrapped yarn and production method thereof
CN104831376A (en) Method for producing fine-denier glazed super-black terylene FDY (Fully Drawn Yarn) filament yarn
CN102747438A (en) Production method for 20D/24F complete-extinction nylon 6 fully-drawn yarn
CN102031575A (en) Method for preparing superfine denier flat terylene drawn yarn
CN104480556A (en) Production process of high-speed spinning type potential crinkled polyester filament yarns
CN106435781B (en) A kind of moisture absorption is ventilative to imitate numb nylon fibre and preparation method thereof
CN109234820A (en) A kind of preparation method of polylactic acid short-fiber
CN107988646A (en) A kind of 66 industrial yarn of semi-dull polyamide fibre and preparation method thereof
CN104831402A (en) Black flame-retardant terylene FDY filament and production method thereof
CN109023564A (en) A kind of preparation method of polylactic acid coloured cut staple
CN103590140B (en) A kind of imitative multiple polyisocyanate of linen look is combined short fibre and manufacture method thereof
CN102912461A (en) Method for producing antibacterial fire-resistant polyester filaments by utilizing recycled polyester bottle chips
CN115012050A (en) Production process of PHBV and PLA blended bio-based fiber
CN110067032A (en) The preparation method of trilobal cross polylactic acid pattern fiber
CN104831381A (en) Production method of glazed extra-black trefoil polyester FDY (Fully Drawn Yarn)
CN104831375A (en) Dull polyester FDY (fully drawn yarn) slub filament yarn and production method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20150812