CN103668491A - Method for producing anti-pilling acrylic fibers - Google Patents
Method for producing anti-pilling acrylic fibers Download PDFInfo
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- CN103668491A CN103668491A CN201210359094.2A CN201210359094A CN103668491A CN 103668491 A CN103668491 A CN 103668491A CN 201210359094 A CN201210359094 A CN 201210359094A CN 103668491 A CN103668491 A CN 103668491A
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Abstract
A method for producing anti-pilling acrylic fibers comprises the steps that (1) polyacrylonitrile polymers are dissolved in sodium thiocyanate aqueous solutions with concentration of 40%-60% through a dissolving machine, the polyacrylonitrile polymers comprise 85%-95% of acrylonitrile, 5%-10% of vinyl acetate and less than 1% of methacrylic acid dimethylamino ethyl ester, and the viscosity average molecular weigh of polyacrylonitrile is 45 thousand to 65 thousand; (2) after spinning solutions are deaerated and filtered, the spinning solutions are metered by a spinning metering pump and are extruded out through spinneret orifices; (3) the spinning solutions are extruded into a coagulating bath through a spinneret plate and form nascent fibers; (4) the fibers enter a secondary coagulating bath to be formed, then cold drafting, washing and hot drafting are carried out, and the total drafting ratio is smaller than or equal to 12; (5) heat drying densifying treatment is carried out on the fibers; (6) heat shaping is carried out on the fibers. The acrylic fibers manufactured through the method have high breakage resistance and pilling resistance.
Description
Technical field
The present invention relates to a kind of production method of wet method Antipilling nitrilon, particularly relate to a kind of production method of anti-pilling acrylic fiber.
Background technology
Most of synthetic fiber all exist in use " balling-up " this phenomenon.Because the brute force of acrylic fibers is higher than natural fabric, on its product surface, the formation speed of fiber spherolite is greater than exfoliation rates, therefore in the situation that frictional force cannot be eliminated fiber spherolite, formed these fiber spherolites will be retained in fabric face for a long time, thereby affect outward appearance and the snugness of fit of fabric.Exploitation patent documentation both domestic and external about anti-pill fibre is also many, as related to the polyacrylonitrile condensate blend that adopts two kinds of different molecular weights and two single content in the Antipilling nitrilon production method of < publication number >1948567, and to be made into polymer content be 13.5%～14% thick stoste, through deaeration, after filtering, obtain spinning solution and carry out spinning.This method has reduced two single content in polymer and has increased intermolecular density, reduces the activity of molecule segment, increases fiber rigidity and for the fragility of shear action, makes the fiber powder in fabric be difficult for being wound in knot, obtains good ANTIPILLING effect.But the production method complex procedures of this Antipilling nitrilon, first polymerization technique regulates, and need to produce the condensate of different viscosity average molecular weighs, and changes two single content.Two kinds of polymeric proportionings that its less important control mixes.Also to solve two kinds of condensate compatibilities and mixing uniformity.Because different molecular weight condensate compatibility is different, and after dissolving mobility difference to cause solution to mix inhomogeneous, finally easily cause producing unstable, affect fiber quality.And for example in the method for the reduction balling-up property of acrylic fibre of < publication number >1737246, adopt textile impregnation in finishing agent, to improve ANTIPILLING effect.But this method has increased operation on the one hand, increased the blowdown for the treatment of fluid.Therefore this method is that fabric is carried out to impregnation process on the other hand, fabric is had certain selective.And it is not clearly that the ANTIPILLING effect of fabric improves after repeatedly washing.Also has United States Patent (USP) <3,975, it is 50%-70% in spinning solution that the Antipilling nitrilon that 486> describes is controlled sodium sulfocyanate concentration in coagulating bath in producing, and this concentration range sovent diffusion in spinning technique is excessively slow, fibre forming causes normally spinning excessively slowly.United States Patent (USP) <4, the mode of the employing drawing-off for the second time that 205,037> describes is carried out the production of anti-pill fibre, but very fast owing to spinning at present speed, design such draft apparatus more difficult, and inconvenient operation, expense is higher.
summary of the invention
The object of the invention is to overcome above-mentioned the deficiencies in the prior art, a kind of production method of anti-pilling acrylic fiber is provided, by regulating the quantity of fiber Hole to produce the acrylic fibers with ANTIPILLING characteristic.
Technical solution of the present invention is as follows:
A production method for anti-pilling acrylic fiber, its feature is, it is as follows that the method comprising the steps of:
1. by acrylonitrile content 85%～95%, vinyl acetate content is 5%～10%, dimethylaminoethyl methacrylate content is less than 1%, and the viscosity average molecular weigh of polyacrylonitrile is dissolved in concentration at 4.5 ten thousand～6.5 ten thousand polyacrylonitrile condensate by dissolving machine be in 40%～60% sodium thiocyanate water solution;
2. spinning solution, by after deaeration and filtering, by spinneret orifice is extruded after being measured by spinning pump, and spray orifice can also can be other shape for circle;
3. after spinnerets is clamp-oned coagulating bath, form as-spun fibre, regulate coagulating bath export orientation roller speed and spinnerets extruded velocity, make spinning solution extruded velocity and the ratio of guide roller hauling speed be less than or equal to 5;
4. fiber enters secondary coagulating bath shaping, then carries out cold drawing-off, washing and hot drawing-off, and total draft multiplying power is less than or equal to 12, and fiber heat is dried total contraction and is less than or equal to 20%;
5. fiber carries out heat oven dry densification, 60 ℃～80 ℃ of wet-bulb temperature, 120 ℃～150 ℃ of dry-bulb temperatures;
6. fiber carries out HEAT SETTING, and heat setting temperature is 102 ℃～120 ℃.
Described step 2. in spinning solution polyacrylonitrile condensate content be 7wt % ~ 11wt%, spinning solution temperature is at 30 ℃～50 ℃.More excellent, in spinning solution, polyacrylonitrile condensate content is 8wt % ~ 10wt%.
Described step 3. in coagulating bath sodium sulfocyanate concentration be 10%～15%, be conducive to the diffusion of NaSCN in fiber, and the generation of fiber hole, the temperature of coagulating bath is-2 ℃ ~ 5 ℃.。
Described step 3. middle spinning solution extruded velocity is less than or equal to 4.5 with the ratio of guide roller hauling speed.
Compared with prior art, the invention has the beneficial effects as follows by regulating the quantity of fiber Hole to produce the acrylic fibers with ANTIPILLING characteristic.
The specific embodiment
Below in conjunction with embodiment, the invention will be further described, but should not limit the scope of the invention with this.
A production method for anti-pilling acrylic fiber, comprises that step is as follows:
1. use 40%～60% NaSCN solution, more precisely concentration is dissolved acrylonitrile content 85%～95% at 50%～60% NaSCN solution by high speed dissolving machine, vinyl acetate content is 5%～10%, dimethylaminoethyl methacrylate content is less than 1%, and the viscosity average molecular weigh of polyacrylonitrile is at 4.5 ten thousand～6.5 ten thousand polyacrylonitrile condensate.For guaranteeing better solute effect, Sodium Thiocyanate Solvent need be heated to more than 75 ℃.The Main Function of vinylacetate, for reducing macromolecular chain regularity, reduces molecular rigidity, increases fiber feel.The effect of dimethylaminoethyl methacrylate is mainly to increase dyeing position, and fiber is more easily dyeed.
2. after dissolving, be mixed with condensate content at the spinning solution of 7wt%～12wt%, for improving fiber Hole volume, in spinning solution, condensate scope is preferably 8wt%～11wt%, because condensate content is higher, cause in fiber structure tightr, so fibre strength is high, easily balling-up.Spinning solution is delivered to spinning measuring pump inlet after by deaeration, filtration and temperature-adjustment pressure-adjustment, by measuring pump, after metering, from spinneret orifice, is extruded.
Due to the difference of polymer concentration, so the viscosity of solution and mobility are all different, therefore need to carry out suitable adjustment to solution temperature, make spinning solution temperature be controlled at 30 ℃～50 ℃.We carry out the test of rheological characteristic under different temperatures to the solution of variable concentrations.Result is as shown in the table:
Note: flow graph model MCR301
3. through spinnerets, clamp-on coagulating bath, as-spun fibre carries out double diffusion shaping in coagulating tank.For guaranteeing forming effect and keeping fiber hole, coagulating bath concentration range is arranged between 10%～15%, and temperature range is-2 ℃～5 ℃.For minimizing fiber is sagging and guarantee fiber Hole, regulate coagulating bath export orientation roller speed and spinnerets extruded velocity, make spinning solution extruded velocity and the ratio of guide roller hauling speed be less than or equal to 5, be preferably less than 4.5 times.
4. fiber, after coagulating bath is shaped, enters secondary coagulating bath and is shaped, then enter cold drawing-off, washing and hot drawing-off.For guaranteeing fiber hole, total draft multiple requires to be less than or equal to 12.
5. fiber enters lax densification oven dry after overheated drawing-off, and wherein wet-bulb temperature is set 60 ℃～80 ℃, and dry-bulb temperature is set 120 ℃～150 ℃.
6. fiber carries out HEAT SETTING, and heat setting temperature is 102 ℃～120 ℃.For guaranteeing that fiber has soft feel, after reducing, the generation of yarn filoplume, has certain requirement to the selection of finish.Due to the strong knot of knot, stretching is certain important indicator of anti-pill fibre, for the hole number in assurance fiber and the ANTIPILLING effect of fiber, requires total contraction of fiber to be less than 20%.
The fiber obtaining is carried out to the test of characteristic index, and fiber spinning is made into the test of carrying out ANTIPILLING progression after cloth.Test result is as following table:
As seen from table, the acrylic fiber of preparing through the inventive method has high resistance to fracture, anti-pilling.
Claims (5)
1. a production method for anti-pilling acrylic fiber, is characterized in that, it is as follows that the method comprising the steps of:
1. by acrylonitrile content 85%～95%, vinyl acetate content is 5%～10%, dimethylaminoethyl methacrylate content is less than 1%, and the viscosity average molecular weigh of polyacrylonitrile is dissolved in concentration at 4.5 ten thousand～6.5 ten thousand polyacrylonitrile condensate by dissolving machine be in 40%～60% sodium thiocyanate water solution;
2. spinning solution, by after deaeration and filtering, by spinneret orifice is extruded after being measured by spinning pump;
3. after spinnerets is clamp-oned coagulating bath, form as-spun fibre, regulate coagulating bath export orientation roller speed and spinnerets extruded velocity, make spinning solution extruded velocity and the ratio of guide roller hauling speed be less than or equal to 5;
4. fiber enters secondary coagulating bath shaping, then carries out cold drawing-off, washing and hot drawing-off, and total draft multiplying power is less than or equal to 12;
5. fiber carries out heat oven dry densification, 60 ℃～80 ℃ of wet-bulb temperature, 120 ℃～150 ℃ of dry-bulb temperatures;
6. fiber carries out HEAT SETTING, and heat setting temperature is 102 ℃～120 ℃.
2. the production method of anti-pilling acrylic fiber according to claim 1, is characterized in that, described step 2. in spinning solution polyacrylonitrile condensate content be 7wt % ~ 12wt%, spinning solution temperature is at 30 ℃～50 ℃.
3. the production method of anti-pilling acrylic fiber according to claim 2, is characterized in that, in described spinning solution, polyacrylonitrile condensate content is 8wt % ~ 10wt%.
4. the production method of anti-pilling acrylic fiber according to claim 1, is characterized in that, described step 3. in coagulating bath sodium sulfocyanate concentration be 10%～15%, the temperature of coagulating bath is-2 ℃ ~ 5 ℃.
5. the production method of anti-pilling acrylic fiber according to claim 1, is characterized in that, described step 3. middle spinning solution extruded velocity is less than or equal to 4.5 with the ratio of guide roller hauling speed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201210359094.2A CN103668491A (en) | 2012-09-25 | 2012-09-25 | Method for producing anti-pilling acrylic fibers |
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| CN201210359094.2A CN103668491A (en) | 2012-09-25 | 2012-09-25 | Method for producing anti-pilling acrylic fibers |
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| CN103668491A true CN103668491A (en) | 2014-03-26 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111893592A (en) * | 2020-07-07 | 2020-11-06 | 山西钢科碳材料有限公司 | Polyacrylonitrile fiber, preparation method thereof and polyacrylonitrile-based carbon fiber |
| CN114302985A (en) * | 2019-08-23 | 2022-04-08 | 三菱化学株式会社 | Acrylic fiber, spun yarn and knitted fabric comprising same |
Citations (5)
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|---|---|---|---|---|
| WO1996039552A1 (en) * | 1995-06-06 | 1996-12-12 | Kenneth Wilkinson | Process and product of acrylonitrile copolymer |
| CN1986916A (en) * | 2006-12-12 | 2007-06-27 | 新华锦集团有限公司 | Modified polyacrylonitrile fiber and its making process and use |
| CN101435119A (en) * | 2008-12-19 | 2009-05-20 | 天津工业大学 | Preparation of modified polyacrylonitrile fibre |
| CN101748498A (en) * | 2008-12-12 | 2010-06-23 | 中国石化上海石油化工股份有限公司 | Method for producing anti-pilling acrylic fiber |
| CN101818386A (en) * | 2010-04-28 | 2010-09-01 | 吉林奇峰化纤股份有限公司 | Preparation method of anti-pilling acrylic fiber |
-
2012
- 2012-09-25 CN CN201210359094.2A patent/CN103668491A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1996039552A1 (en) * | 1995-06-06 | 1996-12-12 | Kenneth Wilkinson | Process and product of acrylonitrile copolymer |
| CN1986916A (en) * | 2006-12-12 | 2007-06-27 | 新华锦集团有限公司 | Modified polyacrylonitrile fiber and its making process and use |
| CN101748498A (en) * | 2008-12-12 | 2010-06-23 | 中国石化上海石油化工股份有限公司 | Method for producing anti-pilling acrylic fiber |
| CN101435119A (en) * | 2008-12-19 | 2009-05-20 | 天津工业大学 | Preparation of modified polyacrylonitrile fibre |
| CN101818386A (en) * | 2010-04-28 | 2010-09-01 | 吉林奇峰化纤股份有限公司 | Preparation method of anti-pilling acrylic fiber |
Non-Patent Citations (1)
| Title |
|---|
| 白渝平，韩风: "共聚法酸性染料可染腈纶的研究发展", 《金山油化纤》 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114302985A (en) * | 2019-08-23 | 2022-04-08 | 三菱化学株式会社 | Acrylic fiber, spun yarn and knitted fabric comprising same |
| CN111893592A (en) * | 2020-07-07 | 2020-11-06 | 山西钢科碳材料有限公司 | Polyacrylonitrile fiber, preparation method thereof and polyacrylonitrile-based carbon fiber |
| CN111893592B (en) * | 2020-07-07 | 2022-10-14 | 山西钢科碳材料有限公司 | Polyacrylonitrile fiber, preparation method thereof and polyacrylonitrile-based carbon fiber |
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Application publication date: 20140326 |