CN102864522A - Large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and production method thereof - Google Patents

Large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and production method thereof Download PDF

Info

Publication number
CN102864522A
CN102864522A CN2012103726637A CN201210372663A CN102864522A CN 102864522 A CN102864522 A CN 102864522A CN 2012103726637 A CN2012103726637 A CN 2012103726637A CN 201210372663 A CN201210372663 A CN 201210372663A CN 102864522 A CN102864522 A CN 102864522A
Authority
CN
China
Prior art keywords
liquid
polypropylene
polyethylene terephthalate
monofilament
roller
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
Application number
CN2012103726637A
Other languages
Chinese (zh)
Other versions
CN102864522B (en
Inventor
马海燕
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.)
Nantong new silk monofilament Polytron Technologies Inc
Original Assignee
马海燕
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 马海燕 filed Critical 马海燕
Priority to CN201210372663.7A priority Critical patent/CN102864522B/en
Publication of CN102864522A publication Critical patent/CN102864522A/en
Application granted granted Critical
Publication of CN102864522B publication Critical patent/CN102864522B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Multicomponent Fibers (AREA)

Abstract

The invention discloses a large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and a production method thereof. The monofilament is characterized in that the polymer is PP and PET blended polyester; the mass ratio of PP to PET is (20:80) to (60:40); the diameter of the monofilament is 0.2-1mm; the strength of the monofilament is not less than 3.5CN/dtex; and the elongation at break is 15-25%. The production method comprises the steps of melt extrusion, cooling, drawing and heat setting, wherein a liquid cooling method is adopted in the step of cooling. The production method is simple in process and is convenient to operate; and the formed fibers have the characteristics of high tenacity, high roundness, high uniformity and the like and have wide range of application.

Description

Major diameter PP-PET core-skin type composite monofilament and production method thereof
Technical field
The present invention relates to a kind of major diameter PP-PET core-skin type composite monofilament and production method thereof.
Background technology
There is defective in existing monofilament at aspect of performances such as intensity, extension at breaks, affects service behaviour and the scope of application.
Summary of the invention
The object of the present invention is to provide a kind of major diameter PP-PET core-skin type composite monofilament and production method thereof of favorable working performance.
Technical solution of the present invention is:
A kind of major diameter PP-PET core-skin type composite monofilament, it is characterized in that: polymer is polypropylene, polyethylene terephthalate blending polyester, and the mass ratio of polypropylene and polyethylene terephthalate is 20:80 ~ 60:40, polypropylene is cortex, polyethylene terephthalate is sandwich layer, filament diameter is 0.2 ~ 1mm, and filament strength 〉=3.5CN/dtex, elongation at break are 15 ~ 25%.
The production method of described major diameter PP-PET core-skin type composite monofilament, comprise composite spinning, cooling, stretching, HEAT SETTING step, it is characterized in that: liquid cooling method is adopted in cooling, to directly advance the liquid feeding tank from the polymer melt of spinneret component ejection, carry out the liquid cools moulding, and the forward and backward Wound-up roller in the liquid case carries liquid outlet tank to enter the postorder operation; Forward and backward Wound-up roller is positioned on the same level, distance between the forward and backward Wound-up roller is 50 ~ 120cm, wherein the temperature of liquid is 30 ~ 60 ℃ in the liquid case, and spinneret component spray silk end is 5cm with the distance of liquid case liquid level, and the roller in the liquid case and the distance of liquid level are 30 ~ 80cm; Liquid in the liquid case is circulation fluid, and the flow of circulation fluid is 25 ~ 250kg/h, and the liquid in the liquid case is water, triethylene glycol liquid or paraffin liquid, the tensile stress≤critical tensile stress of monofilament; One-level hot water draft temperature is 80 ~ 98 ℃, and secondary hot blast draft temperature is 140-180 ℃, and total stretching ratio is 4.0 ~ 6.0 times; Heat setting temperature is 160 ~ 180 ℃.
Technique of the present invention is simple, and is easy to operate, and the fiber of moulding has the characteristics such as high-tenacity, high roundness, high uniformity, and the scope of application is wide.
The invention will be further described below in conjunction with drawings and Examples.
Fig. 1 is the cooling device schematic diagram of one embodiment of the invention.
The specific embodiment
A kind of major diameter PP-PET core-skin type composite monofilament, polymer is polypropylene, polyethylene terephthalate blending polyester, and the mass ratio of polypropylene and polyethylene terephthalate is 20:80 ~ 60:40, polypropylene is cortex, polyethylene terephthalate is sandwich layer, filament diameter is 0.2 ~ 1mm, and filament strength 〉=3.5CN/dtex, elongation at break are 15 ~ 25%.
The production method of described major diameter PP-PET core-skin type composite monofilament, comprise composite spinning, cooling, stretching, HEAT SETTING step, liquid cooling method is adopted in cooling, to directly advance the liquid feeding tank 2 from the polymer melt of spinneret component 1 ejection, carry out the liquid cools moulding, and the forward and backward Wound-up roller 3 in the liquid case, 4 carries liquid outlet tank to enter the postorder operation; Forward and backward Wound-up roller is positioned on the same level, distance between the forward and backward Wound-up roller is 50 ~ 120cm, wherein the temperature of liquid is 30 ~ 60 ℃ in the liquid case, and spinneret component spray silk end is 5cm with the distance of liquid case liquid level, and the roller in the liquid case and the distance of liquid level are 30 ~ 80cm; Liquid in the liquid case is circulation fluid, and the flow of circulation fluid is 25 ~ 250kg/h, and the liquid in the liquid case is water, triethylene glycol liquid or paraffin liquid, the tensile stress≤critical tensile stress of monofilament; One-level hot water draft temperature is 80 ~ 98 ℃, and secondary hot blast draft temperature is 140-180 ℃, and total stretching ratio is 4.0 ~ 6.0 times; Heat setting temperature is 160 ~ 180 ℃.

Claims (2)

1. major diameter PP-PET core-skin type composite monofilament, it is characterized in that: polymer is polypropylene, polyethylene terephthalate blending polyester, and the mass ratio of polypropylene and polyethylene terephthalate is 20:80 ~ 60:40, polypropylene is cortex, polyethylene terephthalate is sandwich layer, filament diameter is 0.2 ~ 1mm, and filament strength 〉=3.5CN/dtex, elongation at break are 15 ~ 25%.
2. the production method of major diameter PP-PET core-skin type composite monofilament according to claim 1, comprise composite spinning, cooling, stretching, HEAT SETTING step, it is characterized in that: liquid cooling method is adopted in cooling, to directly advance the liquid feeding tank from the polymer melt of spinneret component ejection, carry out the liquid cools moulding, and the forward and backward Wound-up roller in the liquid case carries liquid outlet tank to enter the postorder operation; Forward and backward Wound-up roller is positioned on the same level, distance between the forward and backward Wound-up roller is 50 ~ 120cm, wherein the temperature of liquid is 30 ~ 60 ℃ in the liquid case, and spinneret component spray silk end is 5cm with the distance of liquid case liquid level, and the roller in the liquid case and the distance of liquid level are 30 ~ 80cm; Liquid in the liquid case is circulation fluid, and the flow of circulation fluid is 25 ~ 250kg/h, and the liquid in the liquid case is water, triethylene glycol liquid or paraffin liquid, the tensile stress≤critical tensile stress of monofilament; One-level hot water draft temperature is 80 ~ 98 ℃, and secondary hot blast draft temperature is 140-180 ℃, and total stretching ratio is 4.0 ~ 6.0 times; Heat setting temperature is 160 ~ 180 ℃.
CN201210372663.7A 2012-09-29 2012-09-29 Large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and production method thereof Active CN102864522B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210372663.7A CN102864522B (en) 2012-09-29 2012-09-29 Large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and production method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210372663.7A CN102864522B (en) 2012-09-29 2012-09-29 Large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and production method thereof

Publications (2)

Publication Number Publication Date
CN102864522A true CN102864522A (en) 2013-01-09
CN102864522B CN102864522B (en) 2014-04-23

Family

ID=47443642

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210372663.7A Active CN102864522B (en) 2012-09-29 2012-09-29 Large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and production method thereof

Country Status (1)

Country Link
CN (1) CN102864522B (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103911685A (en) * 2014-04-29 2014-07-09 厦门怡龙谷新材料科技有限公司 Novel composite monofilament with skin core structure and large diameter, as well as manufacturing method and application thereof
CN103938294A (en) * 2014-04-04 2014-07-23 吉林省华纺纤维制造有限公司 Method for preparing polypropylene/polyethylene terephthalate (PP/PET) composite short fiber without any smell
CN103993384A (en) * 2013-12-31 2014-08-20 江苏德力化纤有限公司 Flax-like FDY fiber and preparation method thereof
CN103993383A (en) * 2013-12-31 2014-08-20 江苏德力化纤有限公司 Flax-like skin-core composite fiber and preparation method thereof
WO2016197560A1 (en) * 2015-06-10 2016-12-15 南通新帝克单丝科技股份有限公司 Large diameter sheath-core composite monofilament and production method therefor
CN112575396A (en) * 2020-12-22 2021-03-30 南通新帝克单丝科技股份有限公司 High-dpf polyester industrial yarn and production method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07316927A (en) * 1994-05-19 1995-12-05 Unitika Ltd Conjugate yarn suitable for safe net
CN101161874A (en) * 2006-10-10 2008-04-16 马海燕 Core-skin type paper making modeling net filament
CN101974794A (en) * 2010-10-26 2011-02-16 马海燕 Large-diameter high-strength polymer hot melting monofilament and production method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07316927A (en) * 1994-05-19 1995-12-05 Unitika Ltd Conjugate yarn suitable for safe net
CN101161874A (en) * 2006-10-10 2008-04-16 马海燕 Core-skin type paper making modeling net filament
CN101974794A (en) * 2010-10-26 2011-02-16 马海燕 Large-diameter high-strength polymer hot melting monofilament and production method thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
马海燕等: "高特PET-PBT共混单丝的结构与性能", 《功能高分子学报》, vol. 24, no. 2, 30 June 2011 (2011-06-30) *

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103993384A (en) * 2013-12-31 2014-08-20 江苏德力化纤有限公司 Flax-like FDY fiber and preparation method thereof
CN103993383A (en) * 2013-12-31 2014-08-20 江苏德力化纤有限公司 Flax-like skin-core composite fiber and preparation method thereof
CN103993384B (en) * 2013-12-31 2017-11-14 江苏德力化纤有限公司 One kind imitates numb FDY fiber and preparation method thereof
CN103993383B (en) * 2013-12-31 2018-01-12 江苏德力化纤有限公司 One kind imitates numb core-skin composite fiber and preparation method thereof
CN103938294A (en) * 2014-04-04 2014-07-23 吉林省华纺纤维制造有限公司 Method for preparing polypropylene/polyethylene terephthalate (PP/PET) composite short fiber without any smell
CN103911685A (en) * 2014-04-29 2014-07-09 厦门怡龙谷新材料科技有限公司 Novel composite monofilament with skin core structure and large diameter, as well as manufacturing method and application thereof
WO2016197560A1 (en) * 2015-06-10 2016-12-15 南通新帝克单丝科技股份有限公司 Large diameter sheath-core composite monofilament and production method therefor
CN112575396A (en) * 2020-12-22 2021-03-30 南通新帝克单丝科技股份有限公司 High-dpf polyester industrial yarn and production method thereof

Also Published As

Publication number Publication date
CN102864522B (en) 2014-04-23

Similar Documents

Publication Publication Date Title
CN102864522B (en) Large-diameter PP-PET (polypropylene-polyethylene terephthalate) sheath-core composite monofilament and production method thereof
CN102864517B (en) High-strength wear-resistant nano-modified polyamide monofilament and production method thereof
CN101230501B (en) Method for preparing high-strength polyethylene fibre by employing blended melting of super high molecular weight polyethylene and low density polyethylene
CN100585035C (en) Core-skin type composite fiber and production method thereof
CN104451917B (en) A kind of production method of chinlon mother's silk
CN103741254B (en) A kind of large-diameter biodegradable polylactic acid monofilament and production method thereof
CN103741253B (en) A kind of large-diameter polymer bent filament and production method thereof
CN103305954A (en) Method for preparing ultra-high molecular weight polyethylene fiber
CN106521665A (en) Production method of bright and ultra-coarse denier16f FDY fiber
CN104514037A (en) Production method of high-strength fine-denier lustrous polyester fiber staple fibers
CN104480555A (en) Production process of high-elasticity-feature terylene pre-oriented fibers
CN104213239B (en) The expanded monofilament of large-diameter polymer and production method thereof
CN104233486A (en) Production process of porous fine denier nylon 6 pre-orientation fibers
CN102851780B (en) Large-diameter thermoplastic elastic monofilament and production method thereof
CN104480557A (en) Chinlon 6 high-strength and fine-denier full-drawn yarns with flattened circular section and preparation method thereof
CN103741251B (en) A kind of major diameter high-strength wearable type monofilament polyester of nano modification and production method thereof
CN102888669A (en) Production process and process equipment for polyester crimped yarn
CN103741252B (en) A kind of large-diameter polyester monofilament based on resistant to hydrolysis and production method thereof
CN102851781A (en) Large-diameter polyether-ether-ketone monofilament and production method thereof
CN104195671B (en) Major diameter PA6-PET core-skin type composite monofilament and production method thereof
CN108385205A (en) High-strength polyester plastic-steel line and preparation method thereof
CN105274649A (en) Large-diameter PVDF-PA6 skin-core type composite monofilament and production method thereof
KR20170088151A (en) Manufacturing method of high strength synthetic fibers using high molecular weight thermoplastic polymer and synthetic fibers with high tenacity
CN103132161A (en) Fine-diameter stretching combined spinneret orifice
CN103741255B (en) A kind of large-diameter polytrimethylene terephthalate monofilament and production method thereof

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
ASS Succession or assignment of patent right

Owner name: NANTONG NTEC SPECIAL FIBER CO., LTD.

Free format text: FORMER OWNER: MA HAIYAN

Effective date: 20150106

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20150106

Address after: 226000, Gangzha District, Jiangsu City, Gangzha province Nantong port industrial and Trade Park

Patentee after: Nantong new silk monofilament Polytron Technologies Inc

Address before: 226000, Gangzha District, Jiangsu City, Nantong province Nantong Gangzha economic and Trade Zone, the new emperor textile fiber Chemical Co., Ltd.

Patentee before: Ma Haiyan