CN112210845A - Coiled fiber capable of being shaped at high temperature and repeatedly processed and preparation method thereof - Google Patents
Coiled fiber capable of being shaped at high temperature and repeatedly processed and preparation method thereof Download PDFInfo
- Publication number
- CN112210845A CN112210845A CN202010977912.XA CN202010977912A CN112210845A CN 112210845 A CN112210845 A CN 112210845A CN 202010977912 A CN202010977912 A CN 202010977912A CN 112210845 A CN112210845 A CN 112210845A
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- Prior art keywords
- spinning
- melt
- slices
- shaped
- fiber
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- Pending
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 36
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- 238000009987 spinning Methods 0.000 claims abstract description 33
- 239000002994 raw material Substances 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 13
- 238000001035 drying Methods 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 239000006057 Non-nutritive feed additive Substances 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract description 6
- 238000007664 blowing Methods 0.000 claims abstract description 4
- 239000004595 color masterbatch Substances 0.000 claims abstract description 4
- 238000005520 cutting process Methods 0.000 claims abstract description 4
- 238000001125 extrusion Methods 0.000 claims abstract description 4
- 238000005303 weighing Methods 0.000 claims abstract description 4
- 239000007822 coupling agent Substances 0.000 claims description 7
- 238000004043 dyeing Methods 0.000 claims description 7
- 239000003607 modifier Substances 0.000 claims description 7
- 239000011347 resin Substances 0.000 claims description 7
- 229920005989 resin Polymers 0.000 claims description 7
- 239000000155 melt Substances 0.000 claims description 6
- 238000009740 moulding (composite fabrication) Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 229920000728 polyester Polymers 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 4
- 150000004756 silanes Chemical class 0.000 claims description 4
- XFTALRAZSCGSKN-UHFFFAOYSA-M sodium;4-ethenylbenzenesulfonate Chemical compound [Na+].[O-]S(=O)(=O)C1=CC=C(C=C)C=C1 XFTALRAZSCGSKN-UHFFFAOYSA-M 0.000 claims description 4
- 239000000498 cooling water Substances 0.000 claims description 3
- 238000009998 heat setting Methods 0.000 claims description 3
- 238000005259 measurement Methods 0.000 claims description 3
- 230000004580 weight loss Effects 0.000 claims description 3
- 150000001844 chromium Chemical class 0.000 claims 1
- 230000008901 benefit Effects 0.000 abstract description 3
- 238000000465 moulding Methods 0.000 abstract description 3
- 238000007380 fibre production Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 3
- 229910052804 chromium Inorganic materials 0.000 description 3
- 239000011651 chromium Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
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
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
- D01F6/92—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyesters
-
- A—HUMAN NECESSITIES
- A41—WEARING APPAREL
- A41G—ARTIFICIAL FLOWERS; WIGS; MASKS; FEATHERS
- A41G3/00—Wigs
- A41G3/0083—Filaments for making wigs
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D1/00—Treatment of filament-forming or like material
- D01D1/06—Feeding liquid to the spinning head
- D01D1/09—Control of pressure, temperature or feeding rate
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D10/00—Physical treatment of artificial filaments or the like during manufacture, i.e. during a continuous production process before the filaments have been collected
- D01D10/02—Heat treatment
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/088—Cooling filaments, threads or the like, leaving the spinnerettes
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Artificial Filaments (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Abstract
The invention relates to the field of adjustment of chemical fiber production formula processes, in particular to a preparation method of a fiber capable of being shaped at high temperature and repeatedly processed into rolls, which comprises the following steps: s1, uniformly mixing the PCT main material, the color master batch and the processing aid, forming a strip after mixing, cooling and molding, and cutting into slices with regular sizes by a granulator; s2, drying the slices, and controlling the moisture content after drying to be below 80 ppm; s3, weighing the dried slices excessively, and enabling the components in the slices to be melted through a screw extruder according to a certain proportion to form spinning melt; s4, carrying out melt extrusion on the spinning melt, extruding the spinning melt into a raw material pipeline in a spinning box, pressurizing the spinning melt, extruding the spinning melt through a spinning assembly, and slowly cooling the spinning melt by cross air blowing to obtain a spinning fiber bundle; and S5, drawing and cooling the prepared fiber bundle to obtain the finished coiled fiber which can be shaped at high temperature and processed repeatedly. The invention has better heat resistance, can be repeatedly rolled and shaped, can greatly reduce the cost consumption for customers and greatly improve the economic benefit.
Description
Technical Field
The invention relates to the field of adjustment of chemical fiber production formula processes, in particular to a preparation method of a fiber capable of being shaped at a high temperature and being repeatedly processed into rolls.
Background
Some wig fibers in the current market are fiber filaments taking PET and PVC as main raw materials, the fiber filaments made of PVC materials cannot resist high temperature and cannot be rolled at high temperature, and the fiber filaments made of PET materials can resist high temperature but can only bear 170-180 ℃ at most when being rolled and molded, and cannot bear repeated high-temperature molding at the same time.
Disclosure of Invention
In order to develop more differentiated products, make the high-temperature molding of the fiber filament more durable and reduce the cost consumption of customers, the invention aims to provide the hair fiber taking the PCT as the main material, solve the technical problems and meet the higher requirements of customers.
The technical scheme adopted by the invention provides a rolled fiber capable of being shaped at high temperature and repeatedly processed and a preparation method thereof. The main material related to the patent is a polyester PCT material, and because the PCT density is lower than that of PET, the prepared hair fiber is light and has good elasticity and activity, and meanwhile, the PCT material has excellent heat resistance and good processing performance, can be continuously rolled for about ten times and has unique flame retardant property. And proved by experiments, the dyeability is obviously superior to that of PET fibers. The preparation method specifically adopted is as follows:
s1, uniformly mixing the PCT main material, the color master batch and the processing aid in a mixer, forming strips through a double-screw granulator after mixing, cooling and forming in cooling water, and cutting into slices with regular sizes by a granulator; the coupling agent is one or any mixture of organic chromium complex, silanes and titanates; the flow promoter is polyester CBT resin; the dyeing modifier is sodium p-styrene sulfonate;
s2, drying the slices in the step S1 to remove water, wherein the drying temperature is 100 ℃ and 130 ℃, the time is controlled to be 9-13 hours, and the water after drying is controlled to be below 80 ppm;
s3, weighing the dried slices in the step S2 by weight loss measurement, and enabling the components in the slices to be melted through a screw extruder according to a certain proportion to form spinning melt;
s4, spinning the melt in the step S3 at a ratio of 60-120kg/cm2The pressure is used for melt extrusion, the raw material pipeline is extruded into a spinning box body through a screw machine head through a bent pipe, the raw material pipeline is extruded out through a spinning component on the spinning box after being pressurized by a metering pump, and the raw material pipeline passes through a spinning channel and is slowly cooled by cross air blowing to obtain a spinning fiber bundle;
s5, the fiber bundle obtained in the step S4 is drafted, heat-set and cooled to obtain the reeled fiber which can be shaped at high temperature and processed repeatedly.
Further, the processing aid comprises a coupling agent, a fluidity promoter and a dyeing modifier, wherein the coupling agent comprises one or any mixture of organic chromium complex, silanes and titanates; the flow promoter comprises a polyester CBT resin; the dyeing modifier comprises sodium p-styrene sulfonate.
Further, the viscosity of the PCT main material is 0.7 Pa.s.
Further, in the step S2, the moisture content of the dried slice is 40ppm or less.
Further, in step S3, the temperatures of the zones of the screw extruder are respectively:
a first area: 275 ℃ and 285 ℃;
and a second zone: 285 ℃ and 295 ℃;
and (3) three zones: 295-305 ℃;
and (4) four areas: 305 ℃ to 310 ℃;
and a fifth zone: 295-305 ℃;
a sixth zone: 295 ℃ and 305 ℃.
Further, the melt of the spinning in the step S4 is melt-extruded to 80-110kg/cm2. For resin raw materials with poor flowability, the pressure requirement is generally higher, the pressure is too high, the screw rotation speed is required to be faster, the reverse flow of melt in the extruder is increased, the power consumption is increased, and if the pressure is beyond the pressure-resistant range of equipment, accidents can occur.
Further, in step S5, the draft ratio of the fiber bundle is 2.5 to 3.5 times, and more preferably 3.0 times.
The temperature range of the heat setting is preferably 160-190 ℃, and more preferably 170-180 ℃.
Compared with the prior art, the invention has the following advantages:
1. the coiled fiber capable of being shaped at high temperature and repeatedly processed has better heat resistance, so that the product competitiveness is improved, and the economic benefit is greatly improved.
2. The coiling fiber capable of being shaped at high temperature and repeatedly processed can be shaped for multiple times, so that the coiling fiber can be shaped for multiple times, and the cost consumption is greatly reduced for customers.
Detailed Description
The technical solutions of the present invention will be further described below with reference to specific examples to facilitate better understanding for those skilled in the art.
The preparation method of the reeling fiber capable of being shaped at high temperature and repeatedly processed comprises the following steps:
s1, uniformly mixing the PCT main material, the color master batch and the processing aid in a mixer, forming strips through a double-screw granulator after mixing, cooling and forming in cooling water, and cutting into slices with regular sizes by a granulator;
s2, drying the slices in the step S1 to remove water, wherein the drying temperature is 100 ℃ and 130 ℃, the time is controlled to be 9-13 hours, and the water after drying is controlled to be below 80 ppm;
s3, weighing the dried slices in the step S2 by weight loss measurement, and enabling the components in the slices to be just melted by a screw extruder according to a certain proportion to form spinning melt;
s4, spinning the melt in the step S3 at a ratio of 60-120kg/cm2The pressure is used for melt extrusion, the raw material pipeline is extruded into a spinning box body through a screw machine head through a bent pipe, the raw material pipeline is extruded out through a spinning component on the spinning box after being pressurized by a metering pump, and the raw material pipeline passes through a spinning channel and is slowly cooled by cross air blowing to obtain a spinning fiber bundle;
s5, the fiber bundle obtained in the step S4 is drafted, heat-set and cooled to obtain the reeled fiber which can be shaped at high temperature and processed repeatedly. Under the condition of a certain spinning speed, the principle of selecting the stretching ratio is as follows: greater than the natural stretch multiple and less than the breaking stretch multiple. The larger the draft multiple of the precursor is, the larger the breaking strength is, and the smaller the breaking elongation is; the smaller the strand draft ratio, the smaller the breaking strength and the larger the breaking elongation. When the draft multiple is more than 3.5 times, broken filaments and broken filaments are generated. When the stretching ratio is less than 2.5 times, the process requirements cannot be met, and tests show that the stretching ratio is optimal when the stretching ratio is 3.0.
The processing aid comprises a coupling agent, a fluidity promoter and a dyeing modifier, wherein the coupling agent comprises one or any mixture of an organic chromium complex, silanes and titanates; the flow promoter comprises a polyester CBT resin; the dyeing modifier comprises sodium p-styrene sulfonate.
Further, the viscosity of the PCT main material is 0.7 Pa.s.
Further, in the step S2, the moisture content of the dried slice is 40ppm or less.
Further, in step S3, the temperatures of the zones of the screw extruder are respectively:
a first area: 275 ℃ and 285 ℃;
and a second zone: 285 ℃ and 295 ℃;
and (3) three zones: 295-305 ℃;
and (4) four areas: 305 ℃ to 310 ℃;
and a fifth zone: 295-305 ℃;
a sixth zone: 295 ℃ and 305 ℃.
Further, the melt of the spinning in the step S4 is melt-extruded to 80-110kg/cm2. For resin raw materials with poor flowability, the pressure requirement is generally higher, the pressure is too high, the screw rotation speed is required to be faster, the reverse flow of melt in the extruder is increased, the power consumption is increased, and if the pressure is beyond the pressure-resistant range of equipment, accidents can occur.
Further, in step S5, the draft ratio of the fiber bundle is 2.5 to 3.5 times, and more preferably 3.0 times.
The temperature range of the heat setting is preferably 160-190 ℃, and more preferably 170-180 ℃.
The above are preferred embodiments of the present invention, and all changes made according to the technical solutions of the present invention that produce functional effects do not exceed the scope of the technical solutions of the present invention belong to the protection scope of the present invention.
Claims (8)
1. A preparation method of a reeled fiber capable of being shaped at high temperature and repeatedly processed is characterized by comprising the following steps:
s1, uniformly mixing the PCT main material, the color master batch and the processing aid in a mixer, forming strips through a double-screw granulator after mixing, cooling and forming in cooling water, and cutting into slices with regular sizes by a granulator;
s2, drying the slices in the step S1 to remove water, wherein the drying temperature is 100 ℃ and 130 ℃, the time is controlled to be 9-13 hours, and the water after drying is controlled to be below 80 ppm;
s3, weighing the dried slices in the step S2 by weight loss measurement, and enabling the components in the slices to be melted through a screw extruder according to a certain proportion to form spinning melt;
s4, spinning the melt in the step S3 at a ratio of 60-120kg/cm2The pressure is used for melt extrusion, the raw material pipeline is extruded into a spinning box body through a screw machine head through a bent pipe, the raw material pipeline is extruded out through a spinning component on the spinning box after being pressurized by a metering pump, and the raw material pipeline passes through a spinning channel and is slowly cooled by cross air blowing to obtain a spinning fiber bundle;
s5, the fiber bundle obtained in the step S4 is drafted, heat-set and cooled to obtain the reeled fiber which can be shaped at high temperature and processed repeatedly.
2. The method for preparing the reeled fiber capable of being shaped at high temperature and being processed repeatedly according to claim 1, wherein the processing aid comprises a coupling agent, a fluidity promoter and a dyeing modifier, wherein the coupling agent comprises one or any mixture of organic chromium complexes, silanes and titanates; the flow promoter comprises a polyester CBT resin; the dyeing modifier comprises sodium p-styrene sulfonate.
3. The method for preparing the reeled fiber capable of being shaped at a high temperature and being processed repeatedly according to claim 1, wherein the viscosity of the PCT main material is 0.7 Pa.s.
4. The method of claim 1, wherein the moisture content of the dried sliced fiber is 40ppm or less in step S2.
5. The method of claim 1, wherein in step S3, the temperatures of the zones of the screw extruder are respectively:
a first area: 275 ℃ and 285 ℃;
and a second zone: 285 ℃ and 295 ℃;
and (3) three zones: 295-305 ℃;
and (4) four areas: 305 ℃ to 310 ℃;
and a fifth zone: 295-305 ℃;
a sixth zone: 295 ℃ and 305 ℃.
6. The method as claimed in claim 1, wherein the melt of the spun yarn is melt-extruded in step S4 to 80-110kg/cm2. For resin raw materials with poor flowability, the pressure requirement is generally higher, the pressure is too high, the screw rotation speed is required to be faster, the reverse flow of melt in the extruder is increased, the power consumption is increased, and if the pressure is beyond the pressure-resistant range of equipment, accidents can occur.
7. The method of claim 1, wherein in step S5, the draft ratio of the fiber bundle is 2.5-3.5 times, and more preferably 3.0 times.
8. The method as claimed in claim 1, wherein the heat setting temperature is preferably in the range of 160-190 ℃, more preferably 170-180 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010977912.XA CN112210845A (en) | 2020-09-17 | 2020-09-17 | Coiled fiber capable of being shaped at high temperature and repeatedly processed and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010977912.XA CN112210845A (en) | 2020-09-17 | 2020-09-17 | Coiled fiber capable of being shaped at high temperature and repeatedly processed and preparation method thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112210845A true CN112210845A (en) | 2021-01-12 |
Family
ID=74049619
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010977912.XA Pending CN112210845A (en) | 2020-09-17 | 2020-09-17 | Coiled fiber capable of being shaped at high temperature and repeatedly processed and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112210845A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112941642A (en) * | 2021-01-12 | 2021-06-11 | 浙江古纤道绿色纤维有限公司 | Colored slice mixing method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101514498A (en) * | 2008-02-21 | 2009-08-26 | Uno有限公司 | Flameproof polyester type synthetic hair filament and method for preparing the same |
| CN104294387A (en) * | 2014-10-31 | 2015-01-21 | 河南瑞贝卡发制品股份有限公司 | PBT/PET blending imitated human hair fiber and preparing method thereof |
| CN109402766A (en) * | 2018-10-12 | 2019-03-01 | 河南瑞贝卡发制品股份有限公司 | Height emulation human hair wig heat resistant polyamide fiber and preparation method thereof |
-
2020
- 2020-09-17 CN CN202010977912.XA patent/CN112210845A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101514498A (en) * | 2008-02-21 | 2009-08-26 | Uno有限公司 | Flameproof polyester type synthetic hair filament and method for preparing the same |
| CN104294387A (en) * | 2014-10-31 | 2015-01-21 | 河南瑞贝卡发制品股份有限公司 | PBT/PET blending imitated human hair fiber and preparing method thereof |
| CN109402766A (en) * | 2018-10-12 | 2019-03-01 | 河南瑞贝卡发制品股份有限公司 | Height emulation human hair wig heat resistant polyamide fiber and preparation method thereof |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112941642A (en) * | 2021-01-12 | 2021-06-11 | 浙江古纤道绿色纤维有限公司 | Colored slice mixing method |
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Application publication date: 20210112 |