CN105951192A - Polyester-polyester hot melt composite filament production method - Google Patents

Polyester-polyester hot melt composite filament production method Download PDF

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Publication number
CN105951192A
CN105951192A CN201610314549.7A CN201610314549A CN105951192A CN 105951192 A CN105951192 A CN 105951192A CN 201610314549 A CN201610314549 A CN 201610314549A CN 105951192 A CN105951192 A CN 105951192A
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CN
China
Prior art keywords
polyester
composite
melt
hot melt
screw extruder
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
CN201610314549.7A
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Chinese (zh)
Inventor
杨忠国
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.)
HAIAN ZHONGSHAN SYNTHETIC FIBER CO Ltd
Original Assignee
HAIAN ZHONGSHAN SYNTHETIC FIBER 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 HAIAN ZHONGSHAN SYNTHETIC FIBER CO Ltd filed Critical HAIAN ZHONGSHAN SYNTHETIC FIBER CO Ltd
Priority to CN201610314549.7A priority Critical patent/CN105951192A/en
Publication of CN105951192A publication Critical patent/CN105951192A/en
Pending legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • D01F8/04Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
    • D01F8/14Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent

Abstract

The invention provides a polyester-polyester hot melt composite filament production method comprising the following steps: 1, using a high melting point polyester slice with the melting point above 260 DEG C as the first raw material entering the first screw extruder, the raw material is fused and extruded by the first screw extruder to form a spinnable polyester melt, the spinnable polyester melt is transferred to a composite spinning box body and further evenly distributed to a composite spinning assembly, thus forming the core of sheath core collar compound filaments; 2, using the low melting point polyester slice, with the softening point between 147 and 172 DEG C, as the second raw material, the second raw material enters the second screw extruder and is fused and extruded to form a spinnable polyester melt, the polyester melt is transferred to the composite spinning box body and further evenly distributed to the composite spinning assembly, thus forming the skin of the sheath core collar compound filaments. The polyester-polyester hot melt composite filament production method is good in product thermal stability, wherein the melt point is about 120 DEG C; the bonding effect is good in a client back end application process, and certain intensity is provided.

Description

A kind of production method washing hot melt composite monofilament
Technical field
The present invention relates to a kind of production method washing hot melt composite monofilament, belong to chemical fibre technical field.
Background technology
Low-melting fiber the earliest, is the polyene hydrogen composite fibre succeeded in developing by Chisso Corporation (JP) 6-32, Nakanoshima 3-chome, Kitaku, Osaka, Japan of Japan.It is a kind of with PP as core, with PE as skin, in industrialization in 1997 years.Chisso Corporation (JP) 6-32, Nakanoshima 3-chome, Kitaku, Osaka, Japan is the pioneer in this field, and has almost monopolized the market of PP-PE and PET-PE fiber.Regrettably, the compatibility of PP and PE and PET, caking property are the most bad, so the application of this fibrid is restricted.In order to solve and the problem of polyester fiber bonding, UNITIKA company of Japan successfully develops Melty copolyester with low melting point product.Subsequently, abroad some esbablished corporations have also begun to the exploitation to other copolyesters series products.
Low-melting point polyester is a kind of random copolymerization modified poly ester with relatively low melting point, is a kind of raw material producing heat-bondable fibre, and fusing point is 150-170 degree, the most domestic relies primarily on import, for high-end clothing patch arm of angle lining and the adhesive tape of automotive trim.
Low-melting fiber, compared with polypropylene, Fypro, can occur flow deformation after the latter is melted, not resilient after cooling, thus heat-shrinkable is very big, and the contraction that low-melting fiber is in its free state is only 5%.Therefore, it can replace polypropylene, polyamide-based PUR in some fields, has the application that its own is unique simultaneously.This products material is easy to get, moderate cost, low cost, and preparation technology is simple, can industrialized production.Low-melting point polyester whether still suffers from wide purposes for fiber weaving aspect for adhesive, and its application is boundless, the most great market competitiveness and application prospect.
In terms of adhesive, mainly it is processed into adhesive tape process for clothing, the bonding etc. of automotive trim, being mainly used in textile yarn, industry weaving, health care, filtration filter material, technical fiber, geotextiles, non-woven fabrics, netting, insulation material in terms of fiber weaving, market income is good.
Prior art is primarily present following weak point: use single hot plate heat-shaping in the existing production UDY Si Hou road drawing-off course of processing, it is impossible to ensureing that the intensity of fiber and percentage elongation index are stable, product quality is not sufficiently stable.
Summary of the invention
In place of it is an object of the invention to overcome the deficiencies in the prior art, it is provided that a kind of production method washing hot melt composite monofilament.
The production method washing hot melt composite monofilament of the present invention, comprises the steps:
1. with fusing point higher than 260 DEG C melt polyester section be the first raw material, enter the first screw extruder, melt extruded through the first screw extruder becomes can the polyester fondant of spinning, and this polyester fondant is transported in composite spinning casing, and be evenly distributed to further in composite spining module, become the core composition of the compound monofilament of the core-skin collar;
2. it is the second raw material with softening point low melting point polyester chip in the range of 147 DEG C-172 DEG C, enter the second screw extruder, melt extruded through the second screw extruder becomes can the polyester fondant of spinning, and this polyester fondant is transported in composite spinning casing, and be evenly distributed to further in composite spining module, become the skin composition of the compound monofilament of the core-skin collar;
3. by two kinds of composition extrusions of molding in composite component, process through preliminary draft, obtain double-component polyester and wash hot melt UDY silk;
4. the double-component polyester obtained is washed hot melt UDY silk is 3.6 4.0 in draft ratio, and temperature of heat plate carries out drawing-off processing in the range of being 70 80 DEG C, obtains double component melting adhered polyester fiber UDY, i.e. washs hot melt composite drafting monofilament.
In described step 1), the melt extruded process of the first screw extruder is provided with the 1-5 section thermal treatment zone, and the heating-up temperature in each district is located between 280-295 DEG C.
Described step 2) in, the melt extruded process of the second screw extruder is provided with the 1-5 section thermal treatment zone, and the heating-up temperature in each district is located between 220-250 DEG C.
Described melt polyester section is 1:1 with the weight ratio of low melting point polyester chip.
The production method washing hot melt composite monofilament of the present invention, the product of production has the following technical effect that Heat stability is good, and fusing point is at about 120 DEG C, and during after client, road uses, bonding effect is relatively good, and has certain intensity.
Detailed description of the invention
Embodiment 1
The production method washing hot melt composite monofilament of the present invention, the raw material and the equipment that are used are as follows:
A: section uses:
The dry section (viscosity: 0.679dl/g, fusing point: 260 DEG C) of spinning-grade high melting point polyester
The dry section (viscosity: 0.758dl/g, fusing point: 147 DEG C-172 DEG C) of spinning-grade low-melting point polyester
Core is made in high melting point polyester section, and low melting point polyester chip does skin, produces according to 1:1 coupon weight type ratio.
B: spinning equipment configures: section crystallizing and drying system, composite spinning casing, composite spining module.
C: winding apparatus configures: VC406 type winding apparatus
D: rear road process equipment: VC443 type or KV505 type drafting machine (heating plate device need to be installed additional)
The production method washing hot melt composite monofilament of the present invention, comprises the steps:
1. cutting into slices higher than the high melting point polyester of 260 DEG C of scopes with the fusing point that consumption is 50% weight portion is the first raw material, enter the first screw extruder, melt extruded through the first screw extruder becomes can the polyester fondant of spinning, the melt extruded process of the first screw extruder is provided with 15 sections of thermals treatment zone, the heating-up temperature in each district is located between 280-295 DEG C, and this polyester fondant is transported in composite spinning casing, and be evenly distributed to further in composite spining module, become the core composition of the compound monofilament of the core-skin collar.
2. it is the second raw material with fusing point that consumption is 50% weight portion at 147 DEG C-172 DEG C interior low melting point polyester chips, enter the second screw extruder, melt extruded through the second screw extruder becomes can the polyester fondant of spinning, the melt extruded process of the second screw extruder is provided with 15 sections of thermals treatment zone, the heating-up temperature in each district is located between 220 250 DEG C, and this polyester fondant is transported in composite spinning casing, and be evenly distributed to further in composite spining module, become the skin composition of the compound monofilament of the core-skin collar;
3. by two kinds of composition extrusions of molding in composite component, through including that the preliminary draft of the processes such as cross air blasting cooling molding, oil supply, winding head winding (winding speed is between 600-800m/min) processes, obtain double-component polyester and wash hot melt UDY silk, its fracture strength>1.5cn/dtex, elongation at break is 150 230%, oil point 0PU<1.2%, bar dry<1.0%.
4. the double-component polyester obtained is washed hot melt UDY silk is 3.6 4.0 in draft ratio, temperature of heat plate carries out drawing-off processing in the range of being 70 80 DEG C, obtain double component melting adhered polyester fiber UDY (Chinese: wash hot melt composite drafting monofilament), obtained UDY fracture strength > 4.4cn/dtex, elongation at break is 20 40%.

Claims (4)

1. the production method washing hot melt composite monofilament, it is characterised in that comprise the steps:
1. with fusing point higher than 260 DEG C melt polyester section be the first raw material, enter the first screw extruder, melt extruded through the first screw extruder becomes can the polyester fondant of spinning, and this polyester fondant is transported in composite spinning casing, and be evenly distributed to further in composite spining module, become the core composition of the compound monofilament of the core-skin collar;
2. it is the second raw material with softening point low melting point polyester chip in the range of 147 DEG C-172 DEG C, enter the second screw extruder, melt extruded through the second screw extruder becomes can the polyester fondant of spinning, and this polyester fondant is transported in composite spinning casing, and be evenly distributed to further in composite spining module, become the skin composition of the compound monofilament of the core-skin collar;
3. by two kinds of composition extrusions of molding in composite component, process through preliminary draft, obtain double-component polyester and wash hot melt UDY preliminary draft silk;
4. it is 3.6 4.0 that the double-component polyester obtained washs hot melt UDY silk in draft ratio, hot plate temperature 140 160 DEG C, temperature of heat plate carries out drafting forming processing in the range of being 70 80 DEG C, obtains double component melting adhered polyester fiber UDY long filament, i.e. washs hot melt composite drafting monofilament.
The production method washing hot melt composite monofilament the most according to claim 1, it is characterised in that in described step 1), the melt extruded process of the first screw extruder is provided with the 1-5 section thermal treatment zone, and the heating-up temperature in each district is located between 280-295 DEG C.
The production method washing hot melt composite monofilament the most according to claim 1, it is characterised in that described step 2) in, the melt extruded process of the second screw extruder is provided with the 1-5 section thermal treatment zone, and the heating-up temperature in each district is located between 220-250 DEG C.
The production method washing hot melt composite monofilament the most according to claim 1, it is characterised in that described melt polyester section is 1:1 with the weight ratio of low melting point polyester chip.
CN201610314549.7A 2016-05-13 2016-05-13 Polyester-polyester hot melt composite filament production method Pending CN105951192A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610314549.7A CN105951192A (en) 2016-05-13 2016-05-13 Polyester-polyester hot melt composite filament production method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610314549.7A CN105951192A (en) 2016-05-13 2016-05-13 Polyester-polyester hot melt composite filament production method

Publications (1)

Publication Number Publication Date
CN105951192A true CN105951192A (en) 2016-09-21

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107604474A (en) * 2017-09-19 2018-01-19 旷达纤维科技有限公司 A kind of preparation method of the enhanced colored fibre and fabric of multiconductor welding
CN107988635A (en) * 2017-12-14 2018-05-04 江苏恒力化纤股份有限公司 A kind of full-dull washs composite filament and preparation method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1122853A (en) * 1994-07-04 1996-05-22 智索公司 Hot-melt-adhesive conjugate fibers and a non-woven fabric using the same
CN1344820A (en) * 2001-11-19 2002-04-17 慈溪市大成经营公司 Production process of polyester/polyester composite hot-melt short fiber
CN1519403A (en) * 2003-01-24 2004-08-11 中国人民解放军总后勤部军需装备研究 Hot melting complex fiber and preparation method
JP2008075204A (en) * 2006-09-21 2008-04-03 Unitica Fibers Ltd Thermobondable filament
CN101445972A (en) * 2008-12-29 2009-06-03 浙江理工大学 Method for producing sheath-core type low-melting point polyester staple fiber

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1122853A (en) * 1994-07-04 1996-05-22 智索公司 Hot-melt-adhesive conjugate fibers and a non-woven fabric using the same
CN1344820A (en) * 2001-11-19 2002-04-17 慈溪市大成经营公司 Production process of polyester/polyester composite hot-melt short fiber
CN1519403A (en) * 2003-01-24 2004-08-11 中国人民解放军总后勤部军需装备研究 Hot melting complex fiber and preparation method
JP2008075204A (en) * 2006-09-21 2008-04-03 Unitica Fibers Ltd Thermobondable filament
CN101445972A (en) * 2008-12-29 2009-06-03 浙江理工大学 Method for producing sheath-core type low-melting point polyester staple fiber

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107604474A (en) * 2017-09-19 2018-01-19 旷达纤维科技有限公司 A kind of preparation method of the enhanced colored fibre and fabric of multiconductor welding
CN107988635A (en) * 2017-12-14 2018-05-04 江苏恒力化纤股份有限公司 A kind of full-dull washs composite filament and preparation method thereof

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Application publication date: 20160921