CN109706565A - More feather weight are without tie lines preparation process - Google Patents
More feather weight are without tie lines preparation process Download PDFInfo
- Publication number
- CN109706565A CN109706565A CN201910119411.5A CN201910119411A CN109706565A CN 109706565 A CN109706565 A CN 109706565A CN 201910119411 A CN201910119411 A CN 201910119411A CN 109706565 A CN109706565 A CN 109706565A
- Authority
- CN
- China
- Prior art keywords
- temperature
- raw material
- parts
- cooling
- barrel
- 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
Links
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
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
-
- 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
- D01F8/00—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
- D01F8/04—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
- D01F8/12—Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyamide as constituent
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/02—Yarns or threads characterised by the material or by the materials from which they are made
-
- D—TEXTILES; PAPER
- D02—YARNS; MECHANICAL FINISHING OF YARNS OR ROPES; WARPING OR BEAMING
- D02G—CRIMPING OR CURLING FIBRES, FILAMENTS, THREADS, OR YARNS; YARNS OR THREADS
- D02G3/00—Yarns or threads, e.g. fancy yarns; Processes or apparatus for the production thereof, not otherwise provided for
- D02G3/44—Yarns or threads characterised by the purpose for which they are designed
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Artificial Filaments (AREA)
Abstract
The invention discloses more feather weight without tie lines preparation process, comprising the following steps: 1, raw material mixing;2, dry;3, spinning after the raw material after drying being carried out extrusion molten with screw extruder;4, cooling;5, it oils;6, coiling and molding.For more feather weight of the invention without tie lines preparation process, the nylon wire of preparation has preferable toughness and rigidity, have the advantages that process it is simple, continuously, high production efficiency, stable product quality.
Description
Technical field
The present invention relates to fibre processing technologies field, in particular to more feather weight are without tie lines preparation process.
Background technique
Setline is exactly the line hung on fishing rod when going fishing, very thin but very solid similar to the silk that spider discharge comes.Fishing
Line is commonly used a kind of line in life.Setline not just fishing, however we live in tie up thing also can be with obtaining.
Nylon wire also known as traditional wire, four colo(u)r streaks.The manufacturing process of nylon wire usually takes resin processing to reel off raw silk from cocoons into (biography
System line) and in adding other materials such as color (four colo(u)r streaks) on finished product, characteristic is that have preferable ductility and elasticity.
There are two types of the basic specifications of nylon setline: one is American-European countries's " pound " fixed specification, such as ten pounds of line, it
Maximum pull be able to bear the weight to ten pounds;Another is the setline of Japan's manufacture, usually all with " number " number specification
It distinguishes, there are also Europe manufactures.
Principle is identical with the conception of poundage, about the line of No.1, its maximum pull is able to bear one kilogram of weight, makees
For a kind of standard foundation for drawing fish in water.
Line based on 6 monofilament of nylon is not able to satisfy the multi-field comprehensive use of people increasingly, still has very in performance
The space promoted greatly.
Summary of the invention
The object of the present invention is to provide a kind of more feather weight without tie lines preparation process, using two kinds of materials of nylon 6 and nylon66 fiber
Material is prepared according to a certain percentage, and performance is more superior.
To achieve the above object, the present invention provides more feather weight without tie lines preparation process, comprising the following steps:
1, raw material mixes, and raw material includes the component of following mass fraction: 100 parts of nylon 6 slice, 100-150 parts of nylon 66 slice,
2-10 parts of compatilizer, 20-50 parts of toughener, 0.8-1 parts of auxiliary agent, 0.8-1 parts of dispersing agent, the above raw material is mixed;
2, dry, drying machine is added in mixed raw material or continuous drying tower is dried, 110-125 DEG C of drying temperature, when dry
Between 3.5-4.5 hours, dry vacuum degree is -0.07~-0.09MPa, and the dry moisture content to slice is 750-900ppm;
3, spinning after the raw material after drying being carried out extrusion molten with screw extruder, 180-220 DEG C of spinning melt temperature, spinning
Melt temperature undulated control is at ± 2 DEG C, and the extrusion molten of the screw extruder, area's temperature is 190-200 DEG C, two area's temperature
It is 188-202 DEG C, three area's temperature are 190-205 DEG C, and four area's temperature are 185-199 DEG C;
4, cooling, cross air blowing device is set in blowing duct after spinning and is cooled down, side-blown 0.5 metre per second (m/s) of wind velocity, cross air blasting
19-27 DEG C of air temperature, the humidity of wind is 62-75%;
5, it oils, spinning boundling oils, oil concentration 12.8-14.4%, finish oil applying rate: 0.75-0.95%, range of regulation exist
0.32-2.1 kilograms;
6, coiling and molding, upper draw-off godet frequency: 61-76HZ, winding speed: 979-995 ms/min, lower draw-off godet frequency: 61-
77HZ, friction roller frequency: 68-74HZ, reciprocal frequency of transverse moving: 57-66HZ.
The screw extruder includes rack, and extrusion device is arranged on the rack, and cooling dress is arranged outside extrusion device
It sets, extrusion device includes barrel, screw rod and extrusion die, and feed inlet is arranged on barrel, and screw rod is arranged inside barrel, cooling
Device is arranged on the outside of barrel, and cooling device is that multistage is wrapped in the spiral shape cooling-water duct on the outside of barrel, cooling-water duct
Both ends are respectively water inlet end and water outlet.
Sub-sectional cooling is carried out according to internal zone dividing on the outside of extruder barrel, guarantees that the temperature of each subregion reaches setting and wants
It asks, spiral helicine cooling water pipe, it is cooling uniform, and effect is good.
Wherein when screw extruder extrusion molten, flange temperature is 200-230 DEG C, and spin manifold temperature is 190-205 DEG C, metering
Revolution speed is 14-15 rpms.Extrusion temperature is 210-240 DEG C, revolving speed 200-260rpm, each area's temperature of extrusion process
Spending range is 200~260 DEG C, residence time 1-2 minute, pressure 12-18Mpa.
The compatilizer is selected from ethylene-acrylate-maleic anhydride terpolymer, linear low density polyethylene is grafted
Or mixtures thereof one kind of maleic anhydride, ethylene-octene copolymer grafted maleic anhydride etc..
Processing aid is selected from one or more of low molecule esters, metal soap, the compound esters of stearic acid, amides etc.
Mixture.
Dispersing agent is selected from hydroxypropyl methyl cellulose (HPMC), one of polyacrylamide (PAM) or composition.
Toughener is one of ethylene-acrylic acid copolymer, ethylene-vinyl acetate copolymer, high density ethylene or two
Kind or three kinds.
More feather weight of the invention have preferable toughness and rigidity, have without tie lines preparation process, the nylon wire of preparation
The advantages of process is simple, continuous, high production efficiency, stable product quality.
Detailed description of the invention
Fig. 1 is the structural schematic diagram figure of screw extruder of the present invention.
Specific embodiment
The optimal technical scheme that the invention will now be described in detail with reference to the accompanying drawings.
More feather weight of the invention are without tie lines preparation process, comprising the following steps:
1, raw material mixes, and raw material includes the component of following mass fraction: 100 parts of nylon 6 slice, 120 parts of nylon 66 slice, compatible
5 parts of agent, 40 parts of toughener, 1 part of auxiliary agent, 1 part of dispersing agent, the above raw material is mixed;
2, dry, drying machine is added in mixed raw material or continuous drying tower is dried, 120 DEG C of drying temperature, drying time 4 is small
When, dry vacuum degree is -0.08MPa, and the dry moisture content to slice is 800ppm;
3, spinning after the raw material after drying being carried out extrusion molten with screw extruder, 180-220 DEG C of spinning melt temperature, spinning
Melt temperature undulated control is at ± 2 DEG C, and the extrusion molten of the screw extruder, area's temperature is 190-200 DEG C, two area's temperature
It is 188-202 DEG C, three area's temperature are 190-205 DEG C, and four area's temperature are 185-199 DEG C;
4, cooling, cross air blowing device is set in blowing duct after spinning and is cooled down, side-blown 0.5 metre per second (m/s) of wind velocity, cross air blasting
22 DEG C of air temperature, the humidity of wind is 70%;
5, it oils, spinning boundling oils, oil concentration 13%, finish oil applying rate: 0.85%, range of regulation is at 1 kilogram;
6, coiling and molding, upper draw-off godet frequency: 61-76HZ, winding speed: 979-995 ms/min, lower draw-off godet frequency: 61-
77HZ, friction roller frequency: 68-74HZ, reciprocal frequency of transverse moving: 57-66HZ.
The screw extruder includes rack, and extrusion device is arranged on the rack, and cooling dress is arranged outside extrusion device
It sets, extrusion device includes barrel, screw rod and extrusion die, and feed inlet is arranged on barrel, and screw rod is arranged inside barrel, cooling
Device is arranged on the outside of barrel, and cooling device is that multistage is wrapped in the spiral shape cooling-water duct on the outside of barrel, cooling-water duct
Both ends are respectively water inlet end and water outlet.
Sub-sectional cooling is carried out according to internal zone dividing on the outside of extruder barrel, guarantees that the temperature of each subregion reaches setting and wants
It asks, spiral helicine cooling water pipe, it is cooling uniform, and effect is good.
Wherein when screw extruder extrusion molten, flange temperature is 200-230 DEG C, and spin manifold temperature is 190-205 DEG C, metering
Revolution speed is 14-15 rpms.Extrusion temperature is 210-240 DEG C, revolving speed 200-260rpm, each area's temperature of extrusion process
Spending range is 200~260 DEG C, residence time 1-2 minute, pressure 12-18Mpa.
The compatilizer is selected from ethylene-acrylate-maleic anhydride terpolymer, linear low density polyethylene is grafted
Or mixtures thereof one kind of maleic anhydride, ethylene-octene copolymer grafted maleic anhydride etc..
Processing aid is selected from one or more of low molecule esters, metal soap, the compound esters of stearic acid, amides etc.
Mixture.
Dispersing agent is selected from hydroxypropyl methyl cellulose (HPMC), one of polyacrylamide (PAM) or composition.
Toughener is one of ethylene-acrylic acid copolymer, ethylene-vinyl acetate copolymer, high density ethylene or two
Kind or three kinds.
More feather weight of the invention have preferable toughness and rigidity, have without tie lines preparation process, the nylon wire of preparation
The advantages of process is simple, continuous, high production efficiency, stable product quality.
The copolymerization slice of nylon 6/66 is that a mechanical property is good, and wearability is strong, and fusing point is low, and the in-situ polymerization of plasticizing capacity changes
Property nylon chips, purposes is extremely wide, can be used to make setline.The 50% of total amount is accounted for the setline that 6 monofilament of nylon makes
More than, the copolymerization slice of nylon 6/66 is the ideal spinning raw material of modern setline.
It according to a certain percentage, is produced using two kinds of materials of nylon 6 and nylon66 fiber using in-situ polymerization technology,
The 6 monofilament diameter of nylon spinned with it is thinner, more soft, more wear resistant, more convenient to jettisoning, knot strength more preferably, more resistant to
Water logging, is more suitable for beating various types of fishing line knots, has better ductility compared with PE line with fluorine carbon line, can provide preferably
Buffer function, and there is high tubercle pulling force and straight pull ratio, dyeability is excellent, it is easier to dye various face
Color.
Claims (2)
1. feather weight more than is without tie lines preparation process, it is characterised in that the following steps are included:
1) raw material mixes, and raw material includes the component of following mass fraction: 100 parts of nylon 6 slice, 100-150 parts of nylon 66 slice,
2-10 parts of compatilizer, 20-50 parts of toughener, 0.8-1 parts of auxiliary agent, 0.8-1 parts of dispersing agent, the above raw material is mixed;
2) dry, drying machine is added in mixed raw material or continuous drying tower is dried, 110-125 DEG C of drying temperature, when dry
Between 3.5-4.5 hours, dry vacuum degree is -0.07~-0.09MPa, and the dry moisture content to slice is 750-900ppm;
3) spinning after the raw material after drying being carried out extrusion molten with screw extruder, 180-220 DEG C of spinning melt temperature, spinning
Melt temperature undulated control is at ± 2 DEG C, and the extrusion molten of the screw extruder, area's temperature is 190-200 DEG C, two area's temperature
It is 188-202 DEG C, three area's temperature are 190-205 DEG C, and four area's temperature are 185-199 DEG C;
4) cooling, cross air blowing device is set in blowing duct after spinning and is cooled down, side-blown 0.5 metre per second (m/s) of wind velocity, cross air blasting
19-27 DEG C of air temperature, the humidity of wind is 62-75%;
5) it oils, spinning boundling oils, oil concentration 12.8-14.4%, finish oil applying rate: 0.75-0.95%, range of regulation exist
0.32-2.1 kilograms;
6, coiling and molding, upper draw-off godet frequency: 61-76HZ, winding speed: 979-995 ms/min, lower draw-off godet frequency: 61-
77HZ, friction roller frequency: 68-74HZ, reciprocal frequency of transverse moving: 57-66HZ.
2. more feather weight as described in claim 1 are without tie lines preparation process, it is characterised in that: the screw extruder includes machine
Extrusion device is arranged in frame on the rack, and cooling device is arranged outside extrusion device, and extrusion device includes barrel, screw rod and squeezes
Feed inlet is arranged in die head out on barrel, and screw rod is arranged inside barrel, and cooling device is arranged on the outside of barrel, cooling device
It is wrapped in the spiral shape cooling-water duct on the outside of barrel for multistage, cooling-water duct both ends are respectively water inlet end and water outlet.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910119411.5A CN109706565A (en) | 2019-02-18 | 2019-02-18 | More feather weight are without tie lines preparation process |
PCT/CN2019/087566 WO2020168642A1 (en) | 2019-02-18 | 2019-05-20 | Multi-kilogram-level knotless thread preparation process |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910119411.5A CN109706565A (en) | 2019-02-18 | 2019-02-18 | More feather weight are without tie lines preparation process |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109706565A true CN109706565A (en) | 2019-05-03 |
Family
ID=66264463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910119411.5A Pending CN109706565A (en) | 2019-02-18 | 2019-02-18 | More feather weight are without tie lines preparation process |
Country Status (2)
Country | Link |
---|---|
CN (1) | CN109706565A (en) |
WO (1) | WO2020168642A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020168642A1 (en) * | 2019-02-18 | 2020-08-27 | 海安县中祥线业有限公司 | Multi-kilogram-level knotless thread preparation process |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1998042900A1 (en) * | 1997-03-20 | 1998-10-01 | Rhodia Filtec Ag | Method for producing polyamide monofilaments and monofilament for technical fabric |
CN1237878A (en) * | 1996-11-22 | 1999-12-08 | 巴斯福股份公司 | Long lines |
CN102090382A (en) * | 2010-12-17 | 2011-06-15 | 东莞市协永福实业有限公司 | Method for improving strength of nylon fishing line after being knotted |
CN104195667A (en) * | 2014-09-15 | 2014-12-10 | 马海燕 | Athletic nylon fishing line and producing method thereof |
CN204172324U (en) * | 2014-09-11 | 2015-02-25 | 东莞市金彩色母有限公司 | A kind of look female extrusion device |
CN104562273A (en) * | 2014-06-25 | 2015-04-29 | 巢湖市荷花渔网有限公司 | Method for processing fishing net thread by nylon |
CN106119998A (en) * | 2016-08-26 | 2016-11-16 | 山东合信科技股份有限公司 | A kind of spinning technique of PA66 undrawn yarn |
CN108866704A (en) * | 2018-07-28 | 2018-11-23 | 安徽省义顺渔网渔具有限公司 | A kind of ageing-resistant fishing lines of high-strength corrosion-resisting |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003250408A (en) * | 2002-03-06 | 2003-09-09 | Toray Monofilament Co Ltd | Fishing line and method for producing the same |
CN202415811U (en) * | 2011-12-31 | 2012-09-05 | 杭州帝凯工业布有限公司 | High-strength nylon 6 industrial filament |
CN109234841A (en) * | 2018-09-11 | 2019-01-18 | 厦门市富众渔具有限公司 | A kind of tuna fishline and preparation method thereof |
CN109706565A (en) * | 2019-02-18 | 2019-05-03 | 海安县中祥线业有限公司 | More feather weight are without tie lines preparation process |
-
2019
- 2019-02-18 CN CN201910119411.5A patent/CN109706565A/en active Pending
- 2019-05-20 WO PCT/CN2019/087566 patent/WO2020168642A1/en active Application Filing
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1237878A (en) * | 1996-11-22 | 1999-12-08 | 巴斯福股份公司 | Long lines |
WO1998042900A1 (en) * | 1997-03-20 | 1998-10-01 | Rhodia Filtec Ag | Method for producing polyamide monofilaments and monofilament for technical fabric |
CN102090382A (en) * | 2010-12-17 | 2011-06-15 | 东莞市协永福实业有限公司 | Method for improving strength of nylon fishing line after being knotted |
CN104562273A (en) * | 2014-06-25 | 2015-04-29 | 巢湖市荷花渔网有限公司 | Method for processing fishing net thread by nylon |
CN204172324U (en) * | 2014-09-11 | 2015-02-25 | 东莞市金彩色母有限公司 | A kind of look female extrusion device |
CN104195667A (en) * | 2014-09-15 | 2014-12-10 | 马海燕 | Athletic nylon fishing line and producing method thereof |
CN106119998A (en) * | 2016-08-26 | 2016-11-16 | 山东合信科技股份有限公司 | A kind of spinning technique of PA66 undrawn yarn |
CN108866704A (en) * | 2018-07-28 | 2018-11-23 | 安徽省义顺渔网渔具有限公司 | A kind of ageing-resistant fishing lines of high-strength corrosion-resisting |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020168642A1 (en) * | 2019-02-18 | 2020-08-27 | 海安县中祥线业有限公司 | Multi-kilogram-level knotless thread preparation process |
Also Published As
Publication number | Publication date |
---|---|
WO2020168642A1 (en) | 2020-08-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN108660535B (en) | Special fiber forming material for modified ultrahigh molecular weight polyethylene, preparation method thereof and melt spinning fiber forming method | |
CN101792938B (en) | Novel preparation technology of polyoxymethylene fiber | |
CN103590139B (en) | A kind of powerful three-dimensional crimp memory fiber and manufacture method thereof | |
CN100363405C (en) | Continuous fiber reinforced composite materials, its production method and special equipment therefor | |
CN102418169B (en) | Sea-island fibre and preparation method thereof | |
CN103726126B (en) | PET is utilized to produce the method for flat filament | |
CN103030891A (en) | Long glass fiber-reinforced polypropylene composite material and preparation method thereof | |
CN106280429A (en) | A kind of high-performance high rate of extrusion Nylon-66 reinforced with glass fiber compositions | |
CN104480555A (en) | Production process of high-elasticity-feature terylene pre-oriented fibers | |
CN109706565A (en) | More feather weight are without tie lines preparation process | |
CN104630927A (en) | Melt blending spinning black high strength nylon filament and production method thereof | |
CN101798422B (en) | Production method of polypropylene cooling masterbatch | |
CN105401254A (en) | High-strength and high-modulus polyformaldehyde fiber and two-step hot drawing preparation method thereof | |
CN101851798B (en) | Method for preparing fishing poly-blended and modified polypropylene monofilaments | |
CN103147149B (en) | Preparation method of composite monofilament for netting gear manufacture | |
CN207537607U (en) | A kind of color spins fine-denier polyamide fiber silk production equipment | |
CN101302652A (en) | Processing method of coloured terylene monofilament | |
CN105908277A (en) | Spinning process and die head of chinlon 66 monofilament of high-strength and high-precision industry | |
CN103276471B (en) | The preparation method of wear-resisting monofilament for wire-cloth | |
CN110117402A (en) | A kind of preparation method of POM/PLA alloy 3D printing consumptive material | |
CN102086535B (en) | Method for preparing polyvinyl alcohol coarse denier monofilament fiber | |
CN214137269U (en) | Hot cutting machine head for preparing high-concentration master batches | |
CN115216125A (en) | Special anti-broken PET spinning weather-resistant master batch and preparation method thereof | |
CN107988653A (en) | A kind of low melting point high intensity PE-PP core-sheath monofilament and preparation method thereof | |
CN109735912A (en) | The preparation process of PA66 elastic filament |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190503 |
|
RJ01 | Rejection of invention patent application after publication |