CN109763191A - A kind of seaweed polyester fiber and preparation method thereof - Google Patents
A kind of seaweed polyester fiber and preparation method thereof Download PDFInfo
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- CN109763191A CN109763191A CN201811552129.8A CN201811552129A CN109763191A CN 109763191 A CN109763191 A CN 109763191A CN 201811552129 A CN201811552129 A CN 201811552129A CN 109763191 A CN109763191 A CN 109763191A
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- marine algae
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- 229920000728 polyester Polymers 0.000 title claims abstract description 96
- 239000000835 fiber Substances 0.000 title claims abstract description 80
- 238000002360 preparation method Methods 0.000 title claims abstract description 46
- 241001474374 Blennius Species 0.000 title claims abstract description 40
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 38
- 241000195493 Cryptophyta Species 0.000 claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000002994 raw material Substances 0.000 claims abstract description 7
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical group CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 27
- 238000002156 mixing Methods 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 16
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 claims description 15
- DOOTYTYQINUNNV-UHFFFAOYSA-N Triethyl citrate Chemical compound CCOC(=O)CC(O)(C(=O)OCC)CC(=O)OCC DOOTYTYQINUNNV-UHFFFAOYSA-N 0.000 claims description 15
- DKUYEPUUXLQPPX-UHFFFAOYSA-N dibismuth;molybdenum;oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Mo].[Mo].[Bi+3].[Bi+3] DKUYEPUUXLQPPX-UHFFFAOYSA-N 0.000 claims description 15
- 229940008099 dimethicone Drugs 0.000 claims description 15
- 235000013870 dimethyl polysiloxane Nutrition 0.000 claims description 15
- 239000004205 dimethyl polysiloxane Substances 0.000 claims description 15
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 claims description 15
- 239000000661 sodium alginate Substances 0.000 claims description 15
- 235000010413 sodium alginate Nutrition 0.000 claims description 15
- 229940005550 sodium alginate Drugs 0.000 claims description 15
- 238000009987 spinning Methods 0.000 claims description 15
- 239000001069 triethyl citrate Substances 0.000 claims description 15
- VMYFZRTXGLUXMZ-UHFFFAOYSA-N triethyl citrate Natural products CCOC(=O)C(O)(C(=O)OCC)C(=O)OCC VMYFZRTXGLUXMZ-UHFFFAOYSA-N 0.000 claims description 15
- 235000013769 triethyl citrate Nutrition 0.000 claims description 15
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 14
- 235000017281 sodium acetate Nutrition 0.000 claims description 14
- 239000001632 sodium acetate Substances 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 12
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 claims description 10
- 239000004594 Masterbatch (MB) Substances 0.000 claims description 10
- JUJWROOIHBZHMG-UHFFFAOYSA-N Pyridine Chemical compound C1=CC=NC=C1 JUJWROOIHBZHMG-UHFFFAOYSA-N 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 10
- 230000001112 coagulating effect Effects 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 5
- 239000005977 Ethylene Substances 0.000 claims description 5
- 230000015271 coagulation Effects 0.000 claims description 5
- 238000005345 coagulation Methods 0.000 claims description 5
- 125000005395 methacrylic acid group Chemical group 0.000 claims description 5
- 238000012545 processing Methods 0.000 claims description 5
- UMJSCPRVCHMLSP-UHFFFAOYSA-N pyridine Natural products COC1=CC=CN=C1 UMJSCPRVCHMLSP-UHFFFAOYSA-N 0.000 claims description 5
- 230000004048 modification Effects 0.000 claims description 3
- 238000012986 modification Methods 0.000 claims description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims 1
- 238000001125 extrusion Methods 0.000 claims 1
- 229910052708 sodium Inorganic materials 0.000 claims 1
- 239000011734 sodium Substances 0.000 claims 1
- 238000009835 boiling Methods 0.000 abstract description 10
- 238000010521 absorption reaction Methods 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 3
- 230000008901 benefit Effects 0.000 description 5
- 239000004753 textile Substances 0.000 description 5
- 241000721047 Danaus plexippus Species 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 150000004676 glycans Chemical class 0.000 description 4
- 230000008676 import Effects 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000002074 melt spinning Methods 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 229920001282 polysaccharide Polymers 0.000 description 4
- 239000005017 polysaccharide Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- GVJHHUAWPYXKBD-UHFFFAOYSA-N (±)-α-Tocopherol Chemical compound OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1C GVJHHUAWPYXKBD-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 230000002045 lasting effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000012209 synthetic fiber Substances 0.000 description 2
- 229920002994 synthetic fiber Polymers 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- 102000009027 Albumins Human genes 0.000 description 1
- 108010088751 Albumins Proteins 0.000 description 1
- 241000512259 Ascophyllum nodosum Species 0.000 description 1
- 235000019750 Crude protein Nutrition 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 229930003427 Vitamin E Natural products 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- WIGCFUFOHFEKBI-UHFFFAOYSA-N gamma-tocopherol Natural products CC(C)CCCC(C)CCCC(C)CCCC1CCC2C(C)C(O)C(C)C(C)C2O1 WIGCFUFOHFEKBI-UHFFFAOYSA-N 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 231100000241 scar Toxicity 0.000 description 1
- 229940046009 vitamin E Drugs 0.000 description 1
- 235000019165 vitamin E Nutrition 0.000 description 1
- 239000011709 vitamin E Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 230000010148 water-pollination Effects 0.000 description 1
- 238000009941 weaving Methods 0.000 description 1
Landscapes
- Chemical Or Physical Treatment Of Fibers (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
The present invention provides a kind of seaweed polyester fiber, it is characterized by: the raw material includes: polyester slice, marine algae extract, modifying agent, regulator, the polyester slice, marine algae extract, modifying agent, regulator mass ratio be 90-110:3.3-5.7:4.1-6.2:3-5.It joined marine algae extract in seaweed polyester fiber prepared by the present invention, therefore make the seaweed polyester fiber of preparation that there is good moisture absorption, skin-friendly.Seaweed polyester fiber prepared by the present invention have it is good it is hygroscopic simultaneously, it may have lower boiling water shrinkage, wherein boiling water shrinkage≤0.5%, solves technology prejudice.
Description
Technical field
The present invention relates to a kind of seaweed polyester fibers and preparation method thereof, belong to fibre technology field.
Background technique
Polyester is as one of three big main force's fibers in synthetic fibers, because its excellent physics and chemical characteristic are answered extensively
For garment material and other non-garment industries.Polyester product since the advent of the world, also Zeng Yiqi drapability is good, intensity is high, very
It includes and all kinds of textiles is weaved as main textile raw material by downstream user.With economic globalization, internationalizationof of market, people
Requirement to clothes is also higher and higher, not only to have comfort, also to have functionality, fabric is just to light, soft, functional
Direction is developed, and composite fibre materials need to be continuously improved performance just to meet requirements of weaving process, and China's polyester industrial is quickly grown, and gathers
Oneself develops to 27,000,000 tons of year ends 2010 from 516.5 ten thousand tons at the beginning of 2000 to ester fiber yield, and average annual growth rate is more than
25%, account for the 66% of global polyester output.
Polyester fiber has become the maximum synthetic fibers kind of yield in chemical fibre, be widely used in clothing, decoration,
The national economy various aspects such as household textiles, fabrics for industrial use and national defence, Industrial Engineering.It 5 years from now on, will also keep fast
Speed increases.But as textile material, polyester fiber also has the shortcomings that obvious.Scientific, efficient, good processing method is selected,
To adaptation and promote the high speed sustainable development morning of polyester fiber most important.
Marine algae extract is a kind of pure natural marine organisms product, inside contains phycocolloid acid, crude protein, multivitamin,
Enzyme and microelement etc.." seaweed " is the general name of the marine algaes such as kelp, seaweed, thallus laminariae, agar, is submarine
Algae.Seaweed can provide sufficient moisture for skin, and calm fatigue, rough skin keep skin fine and smooth, glossy, contained
Vitamin E and albumin can desalinate scar.
With the improvement of living standards, requirement of the people to clothes material is higher and higher, the functionality of fiber is proposed
Higher requirement, Chinese invention patent CN201410165075.5, disclosing patent name is a kind of sodium alginate to polyester fibre
The hydrophilic modification method of dimension, by polyester fiber sodium hydroxide solution in the pre- place of stirring in stirring container under the conditions of 70-90 DEG C
Manage 1h, mechanical stirring, the polyester fibre after terminating obtained hydrophilic modifying finally by graft reaction of the sodium alginate to polyester fiber
Dimension, to achieve the effect that polyester fiber is hydrophilic.From the point of view of the above-mentioned prior art, current most seaweed polyester fiber is all
It is attached on textile fiber by post-processing, but such fiber, with daily use, washing etc., fiber surface changes
Property effect can gradually decline and even disappear, it is functional not lasting.
Simultaneously as being added to marine algae extract, the high-hydrophilic energy of marine algae extract causes the polyester fiber of preparation
The abnormal problem that boiling water shrinkage is higher and dyeing is uneven, affects spinning performance.
Summary of the invention
The problem to be solved in the present invention is against the above deficiency, to provide a kind of seaweed polyester fiber and preparation method thereof, with
Realize following goal of the invention:
1, providing one kind has seaweed polyester fiber, and the seaweed polyester fiber of preparation is made to have lasting hydrophily and skin-friendly.
2, the present invention preparation seaweed polyester fiber while improving hydrophilicity, with lower boiling water shrinkage and compared with
Good dyeability.
3, color difference silk and striped silk is greatly lowered.
In order to solve the above technical problems, the technical solution adopted by the present invention is as follows:
A kind of seaweed polyester fiber, raw material include polyester slice, marine algae extract, modifying agent, regulator;The polyester is cut
Piece, marine algae extract, modifying agent, regulator mass ratio be 90-110:3.3-5.7:4.1-6.2:3-5;
The polyester slice: water content≤0.2%, acetaldehyde≤1%, acid value max.35Meq/kg, intrinsic viscosity 0.865 ±
0.015dl/g is bought by Suzhou benefit monarch at plasticizing Import and Export Co., Ltd., article No.: LJC-CB-608S;The marine algae extract:
Algal polysaccharides content >=50%, moisture content≤0.5%, Xi'an Wei Zhen Biotechnology Co., Ltd produce;
Further, the modifying agent, by triethyl citrate, bismuth molybdate, dimethicone, neopelex group
At;Preferably, in the modifying agent triethyl citrate, bismuth molybdate, dimethicone, neopelex preferred ratio
Example is 12-18:1-2:5-8:0.2-0.5.
Further, the regulator is made of sodium acetate, sodium alginate, isopropanol;
Preferably, sodium acetate, sodium alginate, the preferred mass ratio of isopropanol are according to 5-4:1-2:3-4 in the regulator.
A kind of preparation method of marine algae extract polyester fiber, comprising the following steps:
Step 1: the preparation of modifying agent: by triethyl citrate, bismuth molybdate, dimethicone, neopelex according to
12-18:1-2:5-8:0.2-0.5 mixing, opens stirring, mixing speed 500-700rpm, mixing time 10-20min are obtained
Obtain mixed liquor;Mixed liquor is stood to heating 40-50min under the conditions of 95-99 DEG C, obtains modifying agent.
Step 2: the preparation of regulator: sodium acetate, sodium alginate, isopropanol are mixed according to the mass ratio of 5-4:1-2:3-4
It closes, after mixing evenly, mixed liquor is subjected to microwave treatment, the microwave treatment: power 280-300w, treatment temperature 67-80
DEG C, the processing time is 50-60s, and number of processes is 1-3 times, interval time 2-3min;After microwave treatment, regulator is obtained.
Step 3: the preparation of modified poly ester master batch: polyester slice, marine algae extract, modifying agent to be uniformly mixed and be added to
Melt extruded is carried out in screw extruder and obtains modified poly ester melt, and temperature is 287-293 DEG C.
Step 4: the preparation of spinning solution: modified poly ester master batch being mixed with regulator, is heated to 320-335 DEG C, when heating
Between be 20-30min, stirring rate 400-500rpm;Obtain melt spinning liquid.
Step 5: spinning
Spinning solution is imported in manifold, fiber is sprayed from the hole of spinneret, and the hole cross section of spinneret is equilateral circle, is squeezed
Temperature is 265-272 DEG C out, and subsequently into coagulating bath, coagulation bath temperature is 54-58 DEG C, and ethylene methacrylic pyridine is dense in coagulating bath
Degree is 35-41%, internal circulating load 70-80kL/h;Obtain fibre bundle.
Step 6: drawing-off oils
It obtains fibre bundle and carries out 3 drawing-offs, draw ratio is respectively 1:1.5-1.8,1:1.6-1.8,1:1.08-1.25;Drawing-off
Afterwards, fibre bundle drying, cooling, curl, obtain seaweed polyester fiber.
The invention adopts the above technical scheme, compared with prior art, has the advantages that
1, it joined marine algae extract in seaweed polyester fiber prepared by the present invention, therefore there is the seaweed polyester fiber of preparation
Good moisture absorption, skin-friendly.
2, seaweed polyester fiber prepared by the present invention have it is good it is hygroscopic simultaneously, it may have lower boiling shrinkage
Rate, wherein boiling water shrinkage≤0.5%, solves technology prejudice;In general, during polyester modification, hygroscopic enhancing
Mean the raising of boiling water shrinkage, the present invention is made the seaweed polyester fiber of preparation while being had by the innovation of preparation process
Good hygroscopicity and lower boiling water shrinkage.
3, seaweed polyester fiber prepared by the present invention, has preferable dyeing uniformity, and preparation process reduces color difference silk
With the generation of striped silk, wherein color difference silk reduces about 220% or more, and striped silk reduces about 160% or more.
4, seaweed polyester fiber prepared by the present invention, water retention reach 25-32%.
5, seaweed polyester fiber prepared by the present invention has good good hygroscopicity, and diffusion time of dripping is≤0.3s;It inhales
Core height is vertical 242mm/30min, 223 mm/30min of cross.
Specific embodiment
It should be appreciated that preferred embodiments described herein are only used to illustrate and explain the present invention, it is not used to limit this
Invention.
A kind of seaweed polyester fiber of embodiment 1, raw material includes polyester slice, marine algae extract, modifying agent, regulator;
The polyester slice, marine algae extract, modifying agent, regulator mass ratio be 90:3.3:4.5:5;
The polyester slice: water content≤0.2%, acetaldehyde≤1%, acid value max.35Meq/kg, intrinsic viscosity 0.865 ±
0.015dl/g is bought by Suzhou benefit monarch at plasticizing Import and Export Co., Ltd., article No.: LJC-CB-608S;The marine algae extract:
Algal polysaccharides content >=50%, moisture content≤0.5%;
The modifying agent is made of triethyl citrate, bismuth molybdate, dimethicone, neopelex;It is preferred that
, triethyl citrate in the modifying agent, bismuth molybdate, dimethicone, neopelex are preferably in a proportion of 12:
1:5:0.3.
The preferred mass ratio of sodium acetate, sodium alginate, isopropanol is according to 5:2:3 in regulator.
A kind of preparation method of marine algae extract polyester fiber, comprising the following steps:
Step 1: the preparation of modifying agent: by triethyl citrate, bismuth molybdate, dimethicone, neopelex according to
12:1:5:0.. mixing, opens stirring, and mixing speed 500rpm, mixing time 10min obtain mixed liquor;By mixed liquor
Heating 40min is stood under the conditions of 95 DEG C, obtains modifying agent.
Step 2: the preparation of regulator: sodium acetate, sodium alginate, isopropanol being mixed according to the mass ratio of 5:2:3, stirred
Mix uniformly after, mixed liquor is subjected to microwave treatment, the microwave treatment: power 280w, treatment temperature be 67 DEG C, processing the time be
60s, number of processes are 1 time, interval time 2min;After microwave treatment, regulator is obtained.
Step 3: the preparation of modified poly ester master batch: polyester slice, marine algae extract, modifying agent to be uniformly mixed and be added to
Melt extruded is carried out in screw extruder and obtains modified poly ester melt, and temperature is 287-288 DEG C.
Step 4: the preparation of spinning solution: modified poly ester master batch being mixed with regulator, is heated to 320-323 DEG C, when heating
Between be 20min, stirring rate 400rpm;Obtain melt spinning liquid.
Step 5: spinning
Spinning solution is imported in manifold, fiber is sprayed from the hole of spinneret, and the hole cross section of spinneret is equilateral circle, is squeezed
Temperature is 265 DEG C out, and subsequently into coagulating bath, coagulation bath temperature is 54 DEG C, and the concentration of ethylene methacrylic pyridine is in coagulating bath
35%, internal circulating load 70kL/h;Obtain fibre bundle.
Step 6: drawing-off oils
It obtains fibre bundle and carries out 3 drawing-offs, draw ratio is respectively 1:1.5,1:1.6,1:1.25;After drawing-off, fibre bundle warp
Drying, is curled at cooling, and seaweed polyester fiber is obtained.
A kind of seaweed polyester fiber of embodiment 2, raw material includes polyester slice, marine algae extract, modifying agent, regulator;
The polyester slice, marine algae extract, modifying agent, regulator mass ratio be 110:4.5:5.0:3.5;
The polyester slice: water content≤0.2%, acetaldehyde≤1%, acid value max.35Meq/kg, intrinsic viscosity 0.865 ±
0.015dl/g is bought by Suzhou benefit monarch at plasticizing Import and Export Co., Ltd., article No.: LJC-CB-608S;The marine algae extract:
Algal polysaccharides content >=50%, moisture content≤0.5%;
The modifying agent is made of triethyl citrate, bismuth molybdate, dimethicone, neopelex;It is preferred that
, triethyl citrate in the modifying agent, bismuth molybdate, dimethicone, neopelex are preferably in a proportion of 15:
1:8:0.2.
The regulator is made of sodium acetate, sodium alginate, isopropanol;
Preferably, sodium acetate, sodium alginate, the preferred mass ratio of isopropanol are according to 4:2:3 in the regulator.
A kind of preparation method of marine algae extract polyester fiber, comprising the following steps:
Step 1: the preparation of modifying agent: by triethyl citrate, bismuth molybdate, dimethicone, neopelex according to
15:1:8:0.2 mixing, opens stirring, and mixing speed 5600rpm, mixing time 1min obtain mixed liquor;By mixed liquor
Heating 45min is stood under the conditions of 95 DEG C, obtains modifying agent.
Step 2: the preparation of regulator: sodium acetate, sodium alginate, isopropanol being mixed according to the mass ratio of 4:2:3, stirred
Mix uniformly after, mixed liquor is subjected to microwave treatment, the microwave treatment: power 300w, treatment temperature be 80 DEG C, processing the time be
60s, number of processes are 2 times, interval time 3min;After microwave treatment, regulator is obtained.
Step 3: the preparation of modified poly ester master batch: polyester slice, marine algae extract, modifying agent to be uniformly mixed and be added to
Melt extruded is carried out in screw extruder and obtains modified poly ester melt, and temperature is 290-293 DEG C.
Step 4: the preparation of spinning solution: modified poly ester master batch being mixed with regulator, is heated to 330-335 DEG C, when heating
Between be 30min, stirring rate 500rpm;Obtain melt spinning liquid.
Step 5: spinning
Spinning solution is imported in manifold, fiber is sprayed from the hole of spinneret, and the hole cross section of spinneret is equilateral circle, is squeezed
Temperature is 265-268 DEG C out, and subsequently into coagulating bath, coagulation bath temperature is 54-56 DEG C, and ethylene methacrylic pyridine is dense in coagulating bath
Degree is 35-37%, internal circulating load 70kL/h;Obtain fibre bundle.
Step 6: drawing-off oils
It obtains fibre bundle and carries out 3 drawing-offs, draw ratio is respectively 1:1.8,1:1.6,1:1.08;After drawing-off, fibre bundle warp
Drying, is curled at cooling, and seaweed polyester fiber is obtained.
A kind of seaweed polyester fiber of embodiment 3, raw material includes polyester slice, marine algae extract, modifying agent, regulator;
The polyester slice, marine algae extract, modifying agent, regulator mass ratio be 95:3.8:5.5:3.0;
The polyester slice: water content≤0.2%, acetaldehyde≤1%, acid value max.35Meq/kg, intrinsic viscosity 0.865 ±
0.015dl/g is bought by Suzhou benefit monarch at plasticizing Import and Export Co., Ltd., article No.: LJC-CB-608S;The marine algae extract:
Algal polysaccharides content >=50%, moisture content≤0.5%;
The modifying agent is made of triethyl citrate, bismuth molybdate, dimethicone, neopelex;It is preferred that
, triethyl citrate in the modifying agent, bismuth molybdate, dimethicone, neopelex are preferably in a proportion of 16:
1:6:0.3.
The regulator is made of sodium acetate, sodium alginate, isopropanol;
The preferred mass ratio of sodium acetate, sodium alginate, isopropanol is according to 4:1:4 in the regulator.
A kind of preparation method of marine algae extract polyester fiber, comprising the following steps:
Step 1: the preparation of modifying agent: by triethyl citrate, bismuth molybdate, dimethicone, neopelex according to
16:1:6:0.3 mixing, opens stirring, and mixing speed 5700rpm, mixing time 10min obtain mixed liquor;By mixed liquor
Heating 40min is stood under the conditions of 98-99 DEG C, obtains modifying agent.
Step 2: the preparation of regulator: sodium acetate, sodium alginate, isopropanol being mixed according to the mass ratio of 4:1:4, stirred
After mixing uniformly, mixed liquor is carried out microwave treatment, the microwave treatment: power 280w, treatment temperature are 67-68 DEG C, when processing
Between be 50s, number of processes be 2 times, interval time 2min;After microwave treatment, regulator is obtained.
Step 3: the preparation of modified poly ester master batch: polyester slice, marine algae extract, modifying agent to be uniformly mixed and be added to
Melt extruded is carried out in screw extruder and obtains modified poly ester melt, and temperature is 289-291 DEG C.
Step 4: the preparation of spinning solution: modified poly ester master batch being mixed with regulator, is heated to 320-323 DEG C, when heating
Between be 20min, stirring rate 400rpm;Obtain melt spinning liquid.
Step 5: spinning
Spinning solution is imported in manifold, fiber is sprayed from the hole of spinneret, and the hole cross section of spinneret is equilateral circle, is squeezed
Temperature is 272272 DEG C out, and subsequently into coagulating bath, coagulation bath temperature is 56-58 DEG C, and ethylene methacrylic pyridine is dense in coagulating bath
Degree is 40%, internal circulating load 75kL/h;Obtain fibre bundle.
Step 6: drawing-off oils
It obtains fibre bundle and carries out 3 drawing-offs, draw ratio is respectively 1:1.8,1:1.6,1:1.10;After drawing-off, fibre bundle warp
Drying, is curled at cooling, and seaweed polyester fiber is obtained.
A kind of preparation method of the seaweed polyester fiber of comparative example 4, comprising the following steps:
Using the method for embodiment 2, the component ratio of modifying agent is adjusted to 0, in the case where other process conditions are constant, inspection
Survey the influence to preparation seaweed polyester fiber technique and related preparation;
Wherein: on the basis of the process setting that comparative example 4 is prepared to seaweed polyester fiber;
Through testing, specific technical indicator testing result is as shown in table 1:
Table 1
By in table 1, comparison has good water retention as can be seen that seaweed polyester fiber prepared by the present invention, and water retention reaches
25-32%;After technique of the invention, during the preparation process, color difference silk reduces about 220% or more, and striped silk reduces about 160%
More than.
Seaweed polyester fiber prepared by the present invention has excellent moisture absorption property, while having lower boiling water shrinkage, has
Body Testing index is shown in Table 2
Table 2
As can be seen from Table 2, seaweed polyester fiber prepared by the present invention with it is good it is hygroscopic simultaneously, have compared with
Low boiling water shrinkage≤0.5%;With good good hygroscopicity, diffusion time of dripping is≤0.3s;Wick height be it is vertical >=
242mm/30min, cross >=223 mm/30min.
Unless specifically indicated, ratio of the present invention is mass ratio, and the percentage is mass percent.
Finally, it should be noted that the foregoing is only a preferred embodiment of the present invention, it is not intended to restrict the invention,
Although the present invention is described in detail referring to the foregoing embodiments, for those skilled in the art, still may be used
To modify the technical solutions described in the foregoing embodiments or equivalent replacement of some of the technical features.
All within the spirits and principles of the present invention, any modification, equivalent replacement, improvement and so on should be included in of the invention
Within protection scope.
Claims (9)
1. a kind of seaweed polyester fiber, it is characterised in that: the raw material includes: polyester slice, marine algae extract, modifying agent, tune
Save agent;The modifying agent is made of triethyl citrate, bismuth molybdate, dimethicone, neopelex;It is described to change
Triethyl citrate in property agent, bismuth molybdate, dimethicone, neopelex are preferably in a proportion of 12-18:1-2:5-
8:0.2-0.5.
2. a kind of seaweed polyester fiber according to claim 1, it is characterised in that: the polyester slice: water content≤
0.2%, acetaldehyde≤1%, acid value max.35Meq/kg, 0.865 ± 0.015dl/g of intrinsic viscosity.
3. a kind of seaweed polyester fiber according to claim 1, it is characterised in that: the regulator, by sodium acetate, seaweed
Sour sodium, isopropanol form, and sodium acetate, sodium alginate, the preferred mass ratio of isopropanol are according to 5-4:1-2 in the regulator:
3-4。
4. a kind of preparation method of marine algae extract polyester fiber according to claim 1, it is characterised in that: the modification
The preparation method of agent: by triethyl citrate, bismuth molybdate, dimethicone, neopelex according to 12-18:1-2:
5-8:0.2-0.5 mixing, opens stirring, and mixing speed 500-700rpm, mixing time 10-20min obtain mixed liquor;
Mixed liquor is stood to heating 40-50min under the conditions of 95-99 DEG C.
5. a kind of preparation method of marine algae extract polyester fiber according to claim 1, it is characterised in that: the adjusting
The preparation method of agent: sodium acetate, sodium alginate, isopropanol are mixed according to the mass ratio of 5-4:1-2:3-4, after mixing evenly,
Mixed liquor is subjected to microwave treatment, the microwave treatment: power 280-300w, treatment temperature be 67-80 DEG C, processing the time be
50-60s, number of processes are 1-3 times, interval time 2-3min.
6. a kind of preparation method of marine algae extract polyester fiber according to claim 1, it is characterised in that: the method
Further include the preparation of modified poly ester master batch: polyester slice, marine algae extract, modifying agent being uniformly mixed and are added to screw extruder
Middle progress melt extruded obtains modified poly ester melt, and temperature is 287-293 DEG C.
7. a kind of preparation method of marine algae extract polyester fiber according to claim 1, it is characterised in that: the method
Further include the preparation of spinning solution: modified poly ester master batch being mixed with regulator, is heated to 320-335 DEG C, heating time 20-
30min, stirring rate 400-500rpm.
8. a kind of preparation method of marine algae extract polyester fiber according to claim 1, it is characterised in that: the method
Further include spinning: extrusion temperature is 265-272 DEG C, coagulation bath temperature is 54-58 DEG C, and ethylene methacrylic pyridine is dense in coagulating bath
Degree is 35-41%, internal circulating load 70-80kL/h.
9. a kind of preparation method of marine algae extract polyester fiber according to claim 1, it is characterised in that: the method
Further include drawing-off: draw ratio is respectively 1:1.5-1.8,1:1.6-1.8,1:1.08-1.25.
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