CN106400178B - A kind of manufacturing method of different contraction terylene low stretch yarn - Google Patents

A kind of manufacturing method of different contraction terylene low stretch yarn Download PDF

Info

Publication number
CN106400178B
CN106400178B CN201610796612.5A CN201610796612A CN106400178B CN 106400178 B CN106400178 B CN 106400178B CN 201610796612 A CN201610796612 A CN 201610796612A CN 106400178 B CN106400178 B CN 106400178B
Authority
CN
China
Prior art keywords
parts
different contraction
different
contraction
spinneret orifice
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.)
Active
Application number
CN201610796612.5A
Other languages
Chinese (zh)
Other versions
CN106400178A (en
Inventor
吴金亮
卢年春
吴维光
焦岩岩
赵文球
赵成均
袁剑青
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Rong Xiang Chemical Fiber Co., Ltd.
Original Assignee
Rong Xiang Chemical Fiber Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Rong Xiang Chemical Fiber Co Ltd filed Critical Rong Xiang Chemical Fiber Co Ltd
Priority to CN201610796612.5A priority Critical patent/CN106400178B/en
Publication of CN106400178A publication Critical patent/CN106400178A/en
Application granted granted Critical
Publication of CN106400178B publication Critical patent/CN106400178B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/88Monocomponent 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
    • D01F6/92Monocomponent 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
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/66Polyesters containing oxygen in the form of ether groups
    • C08G63/664Polyesters containing oxygen in the form of ether groups derived from hydroxy carboxylic acids
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/66Polyesters containing oxygen in the form of ether groups
    • C08G63/668Polyesters containing oxygen in the form of ether groups derived from polycarboxylic acids and polyhydroxy compounds
    • C08G63/672Dicarboxylic acids and dihydroxy compounds
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/253Formation of filaments, threads, or the like with a non-circular cross section; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Textile Engineering (AREA)
  • Medicinal Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Artificial Filaments (AREA)

Abstract

The present invention relates to a kind of manufacturing methods of different contraction terylene low stretch yarn, it includes the following steps:1) will organise magnesium hydroxide crystal whisker, organo montmorillonite, organise barium sulphate nano powder, ethylene glycol, propylene glycol, butanediol, P-hydroxybenzoic acid, sodium germanate is mixed and made into the compound alcoholic solution of different contraction;2) will organise wollastonite nano whiskers fiber, mica powder, polyethylene glycol, propylene glycol, butanediol, high-temperature antioxidant 1098, antimony glycol, protonating agent phosphoric acid is mixed and made into different contraction compound accelerant;3) a kind of different contraction modified poly ester is made in different contraction composite multifunction alcoholic solution, different contraction compound accelerant and p-phthalic acid, ethylene glycol copolycondensation, its melt is sprayed by convex shape spinneret orifice, adopts and different contraction terylene low stretch yarn is made through cooling and solidifying mode, low temperature texturing craft.The fiber of this method manufacture has different crystallization, different orientation, different shrinkage, has wool-like effect.

Description

A kind of manufacturing method of different contraction terylene low stretch yarn
Technical field
The present invention relates to modified poly ester spining technology fields, relate in particular to a kind of manufacture of different contraction terylene low stretch yarn Method.
Background technology
Different shrinkage fiber is a kind of fiber generating different shrinkage due to shrinking percentage difference.Compare currently on the market more The different shrinkage fiber seen, polyphyly are made using the method that the long filament of two strands or three bursts different shrinking percentages carries out network plying;Also It is made using the method for side-by-side bicomponent spinning.
Chinese patent 103484967A discloses a kind of copolyesters melt ultrahigh speed and directly spins controllable polyisocyanate contraction composite fiber Preparation method, Chinese patent 102140700A discloses a kind of preparation method of double different contraction combined yarn, Chinese patent 101962838A discloses a kind of preparation method of the different contraction bicomponent filament yarn of terylene super fine, but these fibers belong to network plying Different shrinkage fiber, network plying fiber due between tow cohesive force it is weak, mode of appearance is often very undesirable after contraction.Separately Outside, the uneven of tow is easily caused due to machinery during plying, to the use in road or even final shadow after influence Ring the presentation quality to fabric.
Chinese patent CN1403639 disclose it is a kind of abnormity from texturized polyester, different contraction T400 fibers etc., but this A little fibers belong to side-by-side bicomponent fiber, it is complicated there are manufacturing process the shortcomings of.
Invention content
It is an object of the invention to overcome the shortcomings of the prior art, it is the different receipts of one-component that fiber can be produced by, which providing, Shrinkage fibers have different crystallization, different orientation, different contraction, and mode of appearance is good after the different contraction of fiber, and one kind with wool-like effect is different The manufacturing method of contraction terylene low stretch yarn.
A kind of manufacturing method of different contraction terylene low stretch yarn provided by the invention, it uses following steps:
A mass fraction) is pressed, by the magnesium hydroxide that organises of a diameter of 0.2-5um of 1-2 parts of characterization parameters, length 10-25um Whisker, the 1-2 parts of nano imvites that organise, the 1-2 parts of barium sulphate nano powders that organise, 65-75 parts of ethylene glycol EG, 5-8 parts 1, PDO, 10-15 parts of 1,4-butanediol BDO, 4-6 part P-hydroxybenzoic acid of 3-propanediol, 0.1-0.3 parts of sodium germanate mixing, mixing are molten Liquid closed griding reaction 2-4 hours in 70 DEG C of agitating ball mills, obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 14-16 by 1-2 parts of draw ratios:The wollastonite nano whiskers fiber that organises of 0.5-1.5, 800 mesh mica powder of 1-2 parts, polyethylene glycol PEG, 8-10 parts of 1,3-PDs PDO, 10-15 part that 8-10 parts of molecular weight are 15000 1,4-butanediol BDO, 0.2-0.4 part high-temperature antioxidant 1098,0.2-0.4 parts of antimony glycols, 0.1-0.3 parts of protonating agent phosphoric acid Mixing, closed agitating ball mill griding reaction 1-2 hours under the conditions of 70 DEG C obtain a kind of different contraction compound accelerant, 70 DEG C Heat preservation for standby use when vacuum dehydration to water content is less than 1%;
C) press mass fraction, it is prepared by step A) the compound alcoholic solution of the different contraction of 2-4 parts mixed with 6-8 parts of ethylene glycol, then It is matched with 15-18 parts of terephthalic acid components, and mashing is blended, be heated to 70 DEG C of vacuum dehydrations, when water content is less than 1% When be added to polyplant, esterification 2 hours is carried out at 250 DEG C of temperature, pressure 0.15MPa, in normal pressure esterification-polycondensation rank Section, be continuously added to 1-2 part and prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C reaction 50 minutes, then take out Vacuum carries out polycondensation reaction, until melt viscosity meets the technological requirement of post-processing in 283 DEG C of temperature, absolute pressure 100Pa or less After discharge, be made a kind of different contraction modified poly ester;
D) using different contraction modified poly ester made of step C, for raw material, melt is sprayed by convex shape spinneret orifice, by spray Preoriented yarn is made then by the inhomogeneous cooling curing mode of distribution gradient in ultrashort zone of silence below filament plate, using A kind of different contraction terylene low stretch yarn is made in low temperature texturing craft.
As an improvement:Step D) in spinneret include plate body and more than one spinneret orifice, the spinneret orifice passes through It wears and sets on plate body, arrange in more than one concentric circles between each spinneret orifice, the spinneret orifice is in convex shape.
As an improvement:Uniform intervals are arranged between spinneret orifice on same concentric circles, on each adjacent concentric circles Spinneret orifice is staggered.
As an improvement:The spinneret orifice of the convex shape is axially symmetric structure, and symmetry axis is directed toward the center of circle of concentric circles.
As an improvement:The spinneret orifice of the convex shape includes a short side rectangular opening and a long side rectangular opening, institute It includes lateral short side and longitudinal short side to state short side rectangular opening, and the long side rectangular opening includes lateral long side and longitudinal long side, described Lateral short side and lateral long side fitting setting, the longitudinal direction short side vertical transverse long side setting, longitudinal short side and longitudinal long length of side It is 0.125~0.6mm to spend identical and range, and the transverse direction long side is longer than lateral short side, the length range of the transverse direction short side Length range for 0.04~0.1mm, the transverse direction long side is 0.06~0.3mm.
A kind of manufacturing method of different contraction terylene low stretch yarn provided by the invention, it uses following steps:
A mass fraction) is pressed, by the magnesium hydroxide crystal whisker that organises of a diameter of 2.6um of 1.5 parts of characterization parameters, length 13um, 1.5 parts of nano imvites that organise, 1.5 parts of barium sulphate nano powders that organise, 70 parts of ethylene glycol EG, 6 parts of 1,3-PDs PDO, 10 parts of 1,4-butanediol BDO, 5 parts of P-hydroxybenzoic acid, 0.2 part of sodium germanate mixing, mixed solution is in 70 DEG C of stirring ball-millings Secret closes griding reaction 3 hours, obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 15 by 1.5 parts of draw ratios:The 1 wollastonite nano whiskers fiber that organises, 1.5 part of 800 mesh Mica powder, 8 parts of molecular weight are 15000 polyethylene glycol PEG, 8 parts of 1,3-PD PDO, 15 parts of 1,4-butanediol BDO, 0.3 part 1098,0.2 part of antimony glycol of high-temperature antioxidant, 0.2 part of protonating agent phosphoric acid mixing, closed agitating ball mill under the conditions of 70 DEG C Griding reaction 1.5 hours, obtains a kind of different contraction compound accelerant, keeps the temperature and waits for when 70 DEG C of vacuum dehydrations to water content are less than 1% With;
C) press mass fraction, be prepared by step A) 3 parts of different compound alcoholic solutions of contraction mixed with 7 parts of ethylene glycol, then with 16 Part terephthalic acid component is matched, and mashing is blended, and is heated to 70 DEG C of vacuum dehydrations, is added when water content is less than 1% To polyplant, esterification is carried out at 250 DEG C of temperature, pressure 0.15MPa 2 hours, in normal pressure esterification-polycondensation phase, even It is continuous to be added 1.5 parts and prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C and react 50 minutes, then vacuumize, Polycondensation reaction is carried out in 283 DEG C of temperature, absolute pressure 100Pa or less, until melt viscosity goes out after meeting the technological requirement of post-processing A kind of different contraction modified poly ester is made in material;
D) using different contraction modified poly ester made of step C, for raw material, melt is sprayed by convex shape spinneret orifice, by spray Preoriented yarn is made then by the inhomogeneous cooling curing mode of distribution gradient in ultrashort zone of silence below filament plate, using A kind of different contraction terylene low stretch yarn is made in low temperature texturing craft.
Compared with prior art, the beneficial effects are mainly as follows:1,3-propanediol, 1,4- butanediols plus Enter, increase the spiral arrangement mode of polyester molecule chain methylene, reduce lattice bulk density, so that material is had more preferable transparent Degree, heat resistance and processability, 1,4- butanediols (BDO) crystalline rate can be promoted, improve crystal property, final products made to generate more Good different contraction appearance effect, i.e. lofting effect;P-hydroxybenzoic acid (PHB) can be copolymerized to form a kind of thermotropic liquid crystal with PET Copolyesters, this material not only has high intensity, high-modulus, and has remarkable melt processing fluidity;Whisker is with list The theory of diameter very small (0.1~10um), atomic arrangement high-sequential, intensity close to perfect crystal made of crystalline form growth It is worth, has the fiber condition of certain draw ratio (5-1000), has the function of high intensity, heat-resisting, fire-retardant, antibacterial, conduction, suction wave etc.. Because of several times to tens times of the length of high molecular material macromolecular chain length, a small amount of whisker is added in the polyester, plays increasing By force, the effect of toughening improves the heat resistance of polyester fiber product, also improves the intensity of polyester fiber.Whisker is a kind of reason The polymer modification agent thought, has a wide range of applications field;Organic grade of montmorillonite of nanometer, has higher surface energy and good Good dispersibility, has very strong affinity with high polymer, can promote crystallizing polyester, improve the strength and elongation of polyester fiber.Mica powder is A kind of nonmetallic mineral, containing Multiple components, wherein mainly having SiO2 and Al2O3, content generally contains in 49% or so, Al2O3 Amount is 30% or so.PET intensity containing ultrafine mica powder is high, and deformation is small, keeps the processing fluidity of PET melt good;Sodium germanate It is the effective catalyst of main reaction, and then there is inert to the reaction for generating by-product;Antimony glycol is to be applied to polycondensation of polyester A kind of reaction catalyst the most novel.The different contraction modified poly ester, is than the advantages of conventional polyester, in spinning process It is middle that than conventional polyester energy rapid crystallization, the addition of nanoscale montmorillonite and mica powder improves the hardness and non-deformability of material, So that the modulus of fiber improves, by the way that whisker is added, the degree of orientation, intensity and the hardness of fiber are all significantly improved. The addition of copolymerization component propylene glycol, butanediol improves the compliance of polyester molecule chain so that the fiber spinned has more excellent Good different shrinkage.Different contraction modified poly ester is combined with spinneret orifice of the present invention, spinning technique, makes prepared fibre Dimension has more excellent different contractility.
The fiber that the method for the present invention produces is one-component different shrinkage fiber, has different crystallization, different orientation, different contraction, fine Mode of appearance is good after tieing up different contraction, has unique wool-like effect.
Description of the drawings
Fig. 1 is the structural schematic diagram for the spinneret that the present invention uses;
Fig. 2 is the convex shape spinneret orifice cross section structure schematic diagram of the present invention;
Specific implementation mode
Below in conjunction with specific embodiment, the present invention will be described in detail:A kind of different contraction terylene of the present invention is low The manufacturing method of elater, using following steps:
A mass fraction) is pressed, by the magnesium hydroxide that organises of a diameter of 0.2-5um of 1-2 parts of characterization parameters, length 10-25um Whisker, the 1-2 parts of nano imvites that organise, the 1-2 parts of barium sulphate nano powders that organise, 65-75 parts of ethylene glycol EG, 5-8 parts 1, PDO, 10-15 parts of 1,4-butanediol BDO, 4-6 part P-hydroxybenzoic acid of 3-propanediol, 0.1-0.3 parts of sodium germanate mixing, mixing are molten Liquid closed griding reaction 2-4 hours in 70 DEG C of agitating ball mills, obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 14-16 by 1-2 parts of draw ratios:The wollastonite nano whiskers fiber that organises of 0.5-1.5, 800 mesh mica powder of 1-2 parts, polyethylene glycol PEG, 8-10 parts of 1,3-PDs PDO, 10-15 part that 8-10 parts of molecular weight are 15000 1,4-butanediol BDO, 0.2-0.4 part high-temperature antioxidant 1098,0.2-0.4 parts of antimony glycols, 0.1-0.3 parts of protonating agent phosphoric acid Mixing, closed agitating ball mill griding reaction 1-2 hours under the conditions of 70 DEG C obtain a kind of different contraction compound accelerant, 70 DEG C Heat preservation for standby use when vacuum dehydration to water content is less than 1%;
C) press mass fraction, it is prepared by step A) the compound alcoholic solution of the different contraction of 2-4 parts mixed with 6-8 parts of ethylene glycol, then It is matched with 15-18 parts of terephthalic acid components, and mashing is blended, be heated to 70 DEG C of vacuum dehydrations, when water content is less than 1% When be added to polyplant, esterification 2 hours is carried out at 250 DEG C of temperature, pressure 0.15MPa, in normal pressure esterification-polycondensation rank Section, be continuously added to 1-2 part and prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C reaction 50 minutes, then take out Vacuum carries out polycondensation reaction, until melt viscosity meets the technological requirement of post-processing in 283 DEG C of temperature, absolute pressure 100Pa or less After discharge, be made a kind of different contraction modified poly ester;
D) using different contraction modified poly ester made of step C, for raw material, melt is sprayed by convex shape spinneret orifice, by spray Preoriented yarn is made then by the inhomogeneous cooling curing mode of distribution gradient in ultrashort zone of silence below filament plate, using A kind of different contraction terylene low stretch yarn is made in low temperature texturing craft.
As shown in Figure 1, 2, step D of the present invention) in spinneret include plate body and more than one spinneret orifice, the spinneret Hole is arranged between each spinneret orifice in more than one concentric circles through being arranged on plate body, and the spinneret orifice is in convex shape;Together Uniform intervals are arranged between spinneret orifice on one concentric circles, and the spinneret orifice on each adjacent concentric circles is staggered;The type The spinneret orifice of shape is axially symmetric structure, and symmetry axis is directed toward the center of circle of concentric circles;The spinneret orifice of the convex shape includes a short side Rectangular opening and a long side rectangular opening, the short side rectangular opening include lateral short side and longitudinal short side, the long side rectangular opening packet Include lateral long side and longitudinal long side, the transverse direction short side and lateral long side fitting setting, the longitudinal direction short side vertical transverse long side Setting, longitudinal short side is identical with longitudinal long side length and range is 0.125~0.6mm, and the transverse direction long side is longer than laterally short The length range on side, the transverse direction short side is 0.04~0.1mm, and the length range of the transverse direction long side is 0.06~0.3mm.
Embodiment 1:A kind of manufacturing method of different contraction terylene low stretch yarn, using following steps:
A mass fraction, by the magnesium hydroxide crystal whisker that organises of a diameter of 0.2um of 1 part of characterization parameter, length 10um, 1) are pressed Part organises nano imvite, 1 part of barium sulphate nano powder that organises, 65 parts of ethylene glycol EG, 8 parts of 1,3-PD PDO, 10 parts 1,4-butanediol BDO, 4 parts of P-hydroxybenzoic acid, the mixing of 0.1 part of sodium germanate, mixed solution are ground 70 DEG C of agitating ball mills are closed Mill reaction 2 hours, obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 14 by 1 part of draw ratio:The 0.5 wollastonite nano whiskers fiber that organises, 1 part of 800 mesh cloud Female powder, 8 parts of molecular weight are 15000 polyethylene glycol PEG, 8 parts of 1,3-PD PDO, 15 parts of 1,4-butanediol BDO, 0.2 part of height 1098,0.2 part of antimony glycol of warm antioxidant, 0.1 part of protonating agent phosphoric acid mixing, closed agitating ball mill is ground under the conditions of 70 DEG C Mill reaction 1 hour obtains a kind of different contraction compound accelerant, heat preservation for standby use when 70 DEG C of vacuum dehydrations to water content are less than 1%;
C) press mass fraction, be prepared by step A) 4 parts of different compound alcoholic solutions of contraction mixed with 6 parts of ethylene glycol, then with 16 Part terephthalic acid component is matched, and mashing is blended, and is heated to 70 DEG C of vacuum dehydrations, is added when water content is less than 1% To polyplant, esterification is carried out at 250 DEG C of temperature, pressure 0.15MPa 2 hours, in normal pressure esterification-polycondensation phase, even It is continuous to be added 1 part and prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C and react 50 minutes, then vacuumize, 283 DEG C of temperature, absolute pressure 100Pa or less carry out polycondensation reaction, until melt viscosity discharges after meeting the technological requirement of post-processing, A kind of different contraction modified poly ester is made;
D step C) is used to be made) different contraction modified poly ester for raw material, melt is sprayed by convex shape spinneret orifice, pass through Then by the inhomogeneous cooling curing mode of distribution gradient preoriented yarn is made, then pass through in ultrashort zone of silence below spinneret It crosses low temperature texturing craft and a kind of different contraction terylene low stretch yarn is made;
The sectional dimension of convex shape wire hole described in the present embodiment a is 0.06mm, h 0.6mm, b 0.12mm;Convex shape sprays Wire hole is distributed on spinneret in concentric circles, and convex shape spinneret centerline hole is directed toward spinneret center, convex on different concentric circles Font wire hole is staggered;Using this plate spinning fiber cooling and solidifying mode be that outer shroud is blown, the ends a outwardly, to obtain every The inhomogeneous cooling solidification effect of distribution gradient on silk cross section.
Embodiment 2:A kind of manufacturing method of different contraction terylene low stretch yarn, using following steps:
A mass fraction) is pressed, by the magnesium hydroxide crystal whisker that organises of a diameter of 2.6um of 1.5 parts of characterization parameters, length 13um, 1.5 parts of nano imvites that organise, 1.5 parts of barium sulphate nano powders that organise, 70 parts of ethylene glycol EG, 6 parts of 1,3-PDs PDO, 10 parts of 1,4-butanediol BDO, 5 parts of P-hydroxybenzoic acid, 0.2 part of sodium germanate mixing, mixed solution is in 70 DEG C of stirring ball-millings Secret closes griding reaction 3 hours, obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 15 by 1.5 parts of draw ratios:The 1 wollastonite nano whiskers fiber that organises, 1.5 part of 800 mesh Mica powder, 8 parts of molecular weight are 15000 polyethylene glycol PEG, 8 parts of 1,3-PD PDO, 15 parts of 1,4-butanediol BDO, 0.3 part 1098,0.2 part of antimony glycol of high-temperature antioxidant, 0.2 part of protonating agent phosphoric acid mixing, closed agitating ball mill under the conditions of 70 DEG C Griding reaction 1.5 hours, obtains a kind of different contraction compound accelerant, keeps the temperature and waits for when 70 DEG C of vacuum dehydrations to water content are less than 1% With;
C) press mass fraction, be prepared by step A) 3 parts of different compound alcoholic solutions of contraction mixed with 7 parts of ethylene glycol, then with 16 Part terephthalic acid component is matched, and mashing is blended, and is heated to 70 DEG C of vacuum dehydrations, is added when water content is less than 1% To polyplant, esterification is carried out at 250 DEG C of temperature, pressure 0.15MPa 2 hours, in normal pressure esterification-polycondensation phase, even It is continuous to be added 1.5 parts and prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C and react 50 minutes, then vacuumize, Polycondensation reaction is carried out in 283 DEG C of temperature, absolute pressure 100Pa or less, until melt viscosity goes out after meeting the technological requirement of post-processing A kind of different contraction modified poly ester is made in material;
D step C) is used to be made) different contraction modified poly ester for raw material, melt is sprayed by convex shape spinneret orifice, pass through Then by the inhomogeneous cooling curing mode of distribution gradient preoriented yarn is made, then pass through in ultrashort zone of silence below spinneret It crosses low temperature texturing craft and a kind of different contraction terylene low stretch yarn is made;
The sectional dimension of convex shape wire hole described in the present embodiment a is 0.06mm, h 0.48mm, b 0.12mm;Convex shape Spinneret orifice is distributed on spinneret in concentric circles, convex shape spinneret centerline hole direction spinneret center, on different concentric circles Convex shape wire hole is staggered;It is that outer shroud is blown using the fiber cooling and solidifying mode of this plate spinning, the ends a are outwardly, every to obtain The inhomogeneous cooling solidification effect of distribution gradient on root silk cross section.
Embodiment 3:A kind of manufacturing method of different contraction terylene low stretch yarn, using following steps:
A mass fraction, by the magnesium hydroxide crystal whisker that organises of a diameter of 0.2um of 1 part of characterization parameter, length 25um, 2) are pressed Part organises nano imvite, 2 parts of barium sulphate nano powders that organise, 70 parts of ethylene glycol EG, 5 parts of 1,3-PD PDO, 15 parts 1,4-butanediol BDO, 5 parts of P-hydroxybenzoic acid, the mixing of 0.2 part of sodium germanate, mixed solution are ground 70 DEG C of agitating ball mills are closed Mill reaction 2.5 hours, obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 15 by 1.5 parts of draw ratios:The 1 wollastonite nano whiskers fiber that organises, 1.5 part of 800 mesh Mica powder, 9 parts of molecular weight are 15000 polyethylene glycol PEG, 9 parts of 1,3-PD PDO, 12 parts of 1,4-butanediol BDO, 0.3 part 1098,0.2 part of antimony glycol of high-temperature antioxidant, 0.2 part of protonating agent phosphoric acid mixing, closed agitating ball mill under the conditions of 70 DEG C Griding reaction 1.5 hours, obtains a kind of different contraction compound accelerant, keeps the temperature and waits for when 70 DEG C of vacuum dehydrations to water content are less than 1% With;
C) press mass fraction, it is prepared by step A) 2.5 parts of different compound alcoholic solutions of contraction mixed with 7.5 parts of ethylene glycol, then It is matched with 16 parts of terephthalic acid components, and mashing is blended, be heated to 70 DEG C of vacuum dehydrations, when water content is less than 1% It is added to polyplant, esterification is carried out at 250 DEG C of temperature, pressure 0.15MPa 2 hours, in normal pressure esterification-polycondensation rank Section, is continuously added to 1 part and is prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C and react 50 minutes, then take out true Sky carries out polycondensation reaction, until after melt viscosity meets the technological requirement of post-processing in 283 DEG C of temperature, absolute pressure 100Pa or less A kind of different contraction modified poly ester is made in discharging;
D step C) is used to be made) different contraction modified poly ester for raw material, melt is sprayed by convex shape spinneret orifice, pass through Then by the inhomogeneous cooling curing mode of distribution gradient preoriented yarn is made, then pass through in ultrashort zone of silence below spinneret It crosses low temperature texturing craft and a kind of different contraction terylene low stretch yarn is made;
The sectional dimension of convex shape wire hole described in the present embodiment a is 0.06mm, h 0.6mm, b 0.18mm;Described is convex Font spinneret orifice is distributed on spinneret in concentric circles, and convex shape spinneret centerline hole is directed toward spinneret center, different concentric circles On convex shape wire hole be staggered;Using this plate spinning fiber cooling and solidifying mode be that outer shroud is blown, the ends a outwardly, to obtain Obtain the inhomogeneous cooling solidification effect of distribution gradient on every silk cross section.
Embodiment 4:A kind of manufacturing method of different contraction terylene low stretch yarn, using following steps:
A mass fraction, by the magnesium hydroxide crystal whisker that organises of a diameter of 5um of 2 parts of characterization parameters, length 25um, 2 parts) are pressed Organise nano imvite, 2 parts of barium sulphate nano powders that organise, 75 parts of ethylene glycol EG, 8 parts of 1,3-PD PDO, 15 part 1, 4- butanediols BDO, 6 parts of P-hydroxybenzoic acid, 0.3 part of sodium germanate mixing, mixed solution is in 70 DEG C of closed grindings of agitating ball mill Reaction 4 hours, obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 16 by 2 parts of draw ratios:The 1.5 wollastonite nano whiskers fiber that organises, 1.5 part of 800 mesh Mica powder, 10 parts of molecular weight are 15000 polyethylene glycol PEG, 10 parts of 1,3-PD PDO, 15 parts of 1,4-butanediol BDO, 0.4 Part 1098,0.4 part of antimony glycol of high-temperature antioxidant, 0.3 part of protonating agent phosphoric acid mixing, closed stirring ball-milling under the conditions of 70 DEG C Machine griding reaction 2 hours, obtains a kind of different contraction compound accelerant, keeps the temperature and waits for when 70 DEG C of vacuum dehydrations to water content are less than 1% With;
C) press mass fraction, be prepared by step A) 2 parts of different compound alcoholic solutions of contraction mixed with 8 parts of ethylene glycol, then with 16 Part terephthalic acid component is matched, and mashing is blended, and is heated to 70 DEG C of vacuum dehydrations, is added when water content is less than 1% To polyplant, esterification is carried out at 250 DEG C of temperature, pressure 0.15MPa 2 hours, in normal pressure esterification-polycondensation phase, even It is continuous to be added 2 parts and prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C and react 50 minutes, then vacuumize, 283 DEG C of temperature, absolute pressure 100Pa or less carry out polycondensation reaction, until melt viscosity discharges after meeting the technological requirement of post-processing, A kind of different contraction modified poly ester is made;
D step C) is used to be made) different contraction modified poly ester for raw material, melt is sprayed by convex shape spinneret orifice, pass through Then by the inhomogeneous cooling curing mode of distribution gradient preoriented yarn is made, then pass through in ultrashort zone of silence below spinneret It crosses low temperature texturing craft and a kind of different contraction terylene low stretch yarn is made;
The sectional dimension of convex shape wire hole described in the present embodiment a is 0.06mm, h 0.48mm, b 0.18mm;Described Convex shape spinneret orifice is distributed on spinneret in concentric circles, and convex shape spinneret centerline hole is directed toward spinneret center, different concentric Convex shape wire hole on circle is staggered;Using this plate spinning fiber cooling and solidifying mode be that outer shroud is blown, the ends a outwardly, to Obtain the inhomogeneous cooling solidification effect of distribution gradient on every silk cross section.
Embodiment of the present invention is not limited to embodiment described above, by aforementioned disclosed numberical range, just Arbitrary replacement is carried out in specific embodiment, and so as to obtain numerous embodiment, this is not enumerated.

Claims (6)

1. a kind of manufacturing method of different contraction terylene low stretch yarn, it is characterised in that the manufacturing method uses following steps:
A mass fraction) is pressed, by the magnesium hydroxide crystalline substance that organises of a diameter of 0.2-5um of 1-2 parts of characterization parameters, length 10-25um Must, the 1-2 parts of nano imvites that organise, the 1-2 parts of barium sulphate nano powders that organise, 65-75 parts of ethylene glycol EG, 5-8 parts 1,3- PDO, 10-15 parts of 1,4-butanediol BDO, 4-6 part P-hydroxybenzoic acid of propylene glycol, 0.1-0.3 parts of sodium germanate mixing, mixed solution Closed griding reaction 2-4 hours in 70 DEG C of agitating ball mills, a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use are obtained;
B mass fraction) is pressed, is 14-16 by 1-2 parts of draw ratios:The wollastonite nano whiskers fiber that organises of 0.5-1.5,1-2 parts 800 mesh mica powders, PEG, 8-10 parts of 1,3-PD PDO, 10-15 part Isosorbide-5-Nitraes-of polyethylene glycol that 8-10 parts of molecular weight are 15000 Butanediol BDO, 0.2-0.4 part high-temperature antioxidant 1098,0.2-0.4 parts of antimony glycols, 0.1-0.3 parts of protonating agent phosphoric acid are mixed It closes, closed agitating ball mill griding reaction 1-2 hours under the conditions of 70 DEG C, obtains a kind of different contraction compound accelerant, 70 DEG C true Heat preservation for standby use when sky dehydration to water content is less than 1%;
C) press mass fraction, it is prepared by step A) the compound alcoholic solution of the different contraction of 2-4 parts mixed with 6-8 parts of ethylene glycol, then with 15- 18 parts of terephthalic acid components are matched, and mashing is blended, and are heated to 70 DEG C of vacuum dehydrations, are added when water content is less than 1% Enter to polyplant, esterification 2 hours is carried out at 250 DEG C of temperature, pressure 0.15MPa, in normal pressure esterification-polycondensation phase, 1-2 parts are continuously added to be prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C and react 50 minutes, then take out true Sky carries out polycondensation reaction in 283 DEG C of temperature, absolute pressure 100Pa or less, and a kind of different contraction modified poly ester is made;
D) use made of step C that different contraction modified poly ester is raw material, melt is sprayed by convex shape spinneret orifice, by spinneret Then by the inhomogeneous cooling curing mode of distribution gradient preoriented yarn is made, using low temperature in the ultrashort zone of silence of lower section A kind of different contraction terylene low stretch yarn is made in texturing craft.
2. a kind of manufacturing method of different contraction terylene low stretch yarn according to claim 1, it is characterised in that:Step D) in Spinneret includes plate body (1) and more than one spinneret orifice (2), and the spinneret orifice (2), which is run through, to be arranged on plate body (1), each It arranges in more than one concentric circles between spinneret orifice (2), the spinneret orifice (2) is in convex shape.
3. a kind of manufacturing method of different contraction terylene low stretch yarn according to claim 2, it is characterised in that:Same concentric circles On spinneret orifice (2) between uniform intervals be arranged, the spinneret orifice (2) on each adjacent concentric circles is staggered.
4. a kind of manufacturing method of different contraction terylene low stretch yarn according to claim 2 or 3, it is characterised in that:It is described convex The spinneret orifice (2) of font is axially symmetric structure, and symmetry axis is directed toward the center of circle of concentric circles.
5. a kind of manufacturing method of different contraction terylene low stretch yarn according to claim 2 or 3, it is characterised in that:It is described convex The spinneret orifice (2) of font includes a short side rectangular opening (21) and a long side rectangular opening (22), the short side rectangular opening (21) Including lateral short side (21a) and longitudinal short side (21b), the long side rectangular opening (22) includes lateral long side (22a) and longitudinal length Side (22b), the transverse direction short side (21a) and lateral long side (22a) are bonded setting, and described longitudinal direction short side (21b) vertical transverse is long Side (22a) is arranged, and longitudinal short side (21b) is identical with longitudinal long side (22b) length and range is 0.125~0.6mm, the cross It is longer than lateral short side (21a) to long side (22a), the length range of the transverse direction short side (21a) is 0.04~0.1mm, the cross It is 0.06~0.3mm to the length range of long side (22a).
6. a kind of manufacturing method of different contraction terylene low stretch yarn, it is characterised in that the manufacturing method uses following steps:
A mass fraction, by the magnesium hydroxide crystal whisker that organises of a diameter of 2.6um of 1.5 parts of characterization parameters, length 13um, 1.5) are pressed Part organises nano imvite, 1.5 parts of barium sulphate nano powders that organise, 70 parts of ethylene glycol EG, 6 parts of 1,3-PD PDO, and 10 Part 1,4-butanediol BDO, 5 parts of P-hydroxybenzoic acid, 0.2 part of sodium germanate mixing, mixed solution are closed in 70 DEG C of agitating ball mills Griding reaction 3 hours obtains a kind of compound alcoholic solution of different contraction, 70 DEG C of heat preservation for standby use;
B mass fraction) is pressed, is 15 by 1.5 parts of draw ratios:The 1 wollastonite nano whiskers fiber that organises, 1.5 part of 800 mesh mica Powder, 8 parts of molecular weight are 15000 polyethylene glycol PEG, 8 parts of 1,3-PD PDO, 15 parts of 1,4-butanediol BDO, 0.3 part of high temperature 1098,0.2 part of antimony glycol of antioxidant, 0.2 part of protonating agent phosphoric acid mixing, closed agitating ball mill grinding under the conditions of 70 DEG C Reaction 1.5 hours obtains a kind of different contraction compound accelerant, heat preservation for standby use when 70 DEG C of vacuum dehydrations to water content are less than 1%;
C) press mass fraction, it is prepared by step A) 3 parts of different compound alcoholic solutions of contraction mixed with 7 parts of ethylene glycol, then with 16 parts it is right Terephthalic acid component is matched, and mashing is blended, and is heated to 70 DEG C of vacuum dehydrations, is added to when water content is less than 1% poly- It attaches together and sets, esterification is carried out at 250 DEG C of temperature, pressure 0.15MPa 2 hours, it is continuous to add in normal pressure esterification-polycondensation phase Enter 1.5 parts to be prepared by step B) different contraction compound accelerant, and be warming up to 270 DEG C react 50 minutes, then vacuumize, in temperature 283 DEG C of degree, absolute pressure 100Pa or less carry out polycondensation reaction, and a kind of different contraction modified poly ester is made;
D step C) is used to be made) different contraction modified poly ester for raw material, melt is sprayed by convex shape spinneret orifice, by spinneret Then by the inhomogeneous cooling curing mode of distribution gradient preoriented yarn is made, using low in ultrashort zone of silence below plate A kind of different contraction terylene low stretch yarn is made in warm texturing craft.
CN201610796612.5A 2016-08-31 2016-08-31 A kind of manufacturing method of different contraction terylene low stretch yarn Active CN106400178B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610796612.5A CN106400178B (en) 2016-08-31 2016-08-31 A kind of manufacturing method of different contraction terylene low stretch yarn

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610796612.5A CN106400178B (en) 2016-08-31 2016-08-31 A kind of manufacturing method of different contraction terylene low stretch yarn

Publications (2)

Publication Number Publication Date
CN106400178A CN106400178A (en) 2017-02-15
CN106400178B true CN106400178B (en) 2018-08-03

Family

ID=58001900

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610796612.5A Active CN106400178B (en) 2016-08-31 2016-08-31 A kind of manufacturing method of different contraction terylene low stretch yarn

Country Status (1)

Country Link
CN (1) CN106400178B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109537088B (en) * 2018-11-24 2021-03-23 开氏石化股份有限公司 Method for manufacturing different-shrinkage polyester low-stretch yarns
CN110952167A (en) * 2019-12-07 2020-04-03 杭州东南纺织有限公司 Method for manufacturing different-shrinkage polyester low-stretch yarns
CN115559014B (en) * 2022-09-15 2024-03-08 浙江盛元化纤有限公司 Preparation method of antistatic wool-like polyester filaments

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR0013099A (en) * 1999-08-06 2002-04-30 Eastman Chem Co Fiber, automotive article, and semicrystalline or crystalline polyester
CN101434691A (en) * 2008-12-11 2009-05-20 江苏新民纺织科技股份有限公司 Different-shrinkage copolyester and preparation method thereof
CN102605498B (en) * 2012-03-31 2014-12-10 浙江正凯化纤有限公司 Method for processing different shrinkage color-mixed terylene air deformation yarns
CN103469345B (en) * 2013-09-27 2015-05-27 苏州大学 Co-polyester melt direct spun differential shrinkage composite fiber and method for preparing same

Also Published As

Publication number Publication date
CN106400178A (en) 2017-02-15

Similar Documents

Publication Publication Date Title
CN106400179B (en) A kind of manufacturing method of polyisocyanate low elastic polyester filament resistant to lodging
CN105908282B (en) A kind of preparation method of the Manufacturing Pet Fine Filaments of 33dtex/144f
CN106400178B (en) A kind of manufacturing method of different contraction terylene low stretch yarn
CN109487352B (en) Graphene polylactic acid bi-component composite fiber and preparation method and equipment thereof
CN101671854B (en) Method for producing polyester industrial yarn by one-step method
CN105603568B (en) A kind of modified hollow cotton and preparation method thereof
CN105908283B (en) A kind of semi-dull POY polyster fibre and its processing method
CN102251308B (en) Method for preparing colored light-extinction polyester filament
CN103437018B (en) A kind of production technology of super emulation silk type brocade ammonia air-coating silk
CN102168320A (en) Production technology for producing porous fine denier colored terylene pre-oriented filament by utilizing recycled polyester bottle flakes
CN104805519B (en) Production method of polyamide-6 profiled fiber
CN104451917B (en) A kind of production method of chinlon mother's silk
CN102864507B (en) Preparation method and product of melt direct spinning superfine porous differential polyester fiber
CN105177743A (en) Method for producing fine denier and micro-fine denier flat regenerated polyester filaments by means of regenerated polyester bottle pieces
CN105862152A (en) Production method for high-speed spinning low-stretching high-modulus low-shrinkage polyester industrial filaments
CN102031575A (en) Method for preparing superfine denier flat terylene drawn yarn
CN101787584A (en) Method for preparing continuous polymerization directly-spun high-shrinkage polyester staple fibers
CN104514037B (en) A kind of production method of high-strength fine denier light terylene short fine dimension
CN107641196A (en) Delustering polyester and low-glossiness elastic composite fiber
CN106400180B (en) A kind of manufacturing method of polyisocyanate multifunctional terylene low stretch yarn
WO2018040691A1 (en) Multi-hole ultra-soft superfine denier polyester fibre and preparation method therefor
CN105256398B (en) It is a kind of from crimping polyester drafting silk and preparation method and application
CN106757429A (en) A kind of heat discoloration polypropylene filament yarn DTY and preparation method thereof
CN103484967A (en) Controllable multiple-differential-shrinkage composition fiber made from copolyester melt through ultra-fast direct spinning, and preparation method of composition fiber
CN106968025A (en) A kind of elastic filament of original liquid coloring grey polyamide fibre 6 and its production method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20180620

Address after: 311247 Hongyang Road, Yunong Town, Xiaoshan District, Hangzhou, Zhejiang, 98

Applicant after: Rong Xiang Chemical Fiber Co., Ltd.

Address before: 311247 Hongyang Road, Yunong Town, Xiaoshan District, Hangzhou, Zhejiang, 98

Applicant before: Rongsheng Petrochemical Co., Ltd.

GR01 Patent grant
GR01 Patent grant