CN105506879B - A kind of step fiber opening method of polyester-nylon composite superfine fibre two - Google Patents

A kind of step fiber opening method of polyester-nylon composite superfine fibre two Download PDF

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Publication number
CN105506879B
CN105506879B CN201610032660.7A CN201610032660A CN105506879B CN 105506879 B CN105506879 B CN 105506879B CN 201610032660 A CN201610032660 A CN 201610032660A CN 105506879 B CN105506879 B CN 105506879B
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fibrillation
polyester
superfine fibre
nylon composite
composite superfine
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CN105506879A (en
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臧锡炎
许陶飞
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Wuxi Tianhua Super Clean Technology Co ltd
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SUZHOU TA&A ULTRA CLEAN TECHNOLOGY Co Ltd
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B1/00Applying liquids, gases or vapours onto textile materials to effect treatment, e.g. washing, dyeing, bleaching, sizing or impregnating
    • D06B1/10Applying liquids, gases or vapours onto textile materials to effect treatment, e.g. washing, dyeing, bleaching, sizing or impregnating by contact with a member carrying the treating material
    • D06B1/14Applying liquids, gases or vapours onto textile materials to effect treatment, e.g. washing, dyeing, bleaching, sizing or impregnating by contact with a member carrying the treating material with a roller
    • D06B1/145Applying liquids, gases or vapours onto textile materials to effect treatment, e.g. washing, dyeing, bleaching, sizing or impregnating by contact with a member carrying the treating material with a roller the treating material being kept in the trough formed between two or more rollers
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B23/00Component parts, details, or accessories of apparatus or machines, specially adapted for the treating of textile materials, not restricted to a particular kind of apparatus, provided for in groups D06B1/00 - D06B21/00
    • D06B23/02Rollers
    • D06B23/023Guiding rollers
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
    • D06M11/32Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond
    • D06M11/36Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with oxygen, ozone, ozonides, oxides, hydroxides or percompounds; Salts derived from anions with an amphoteric element-oxygen bond with oxides, hydroxides or mixed oxides; with salts derived from anions with an amphoteric element-oxygen bond
    • D06M11/38Oxides or hydroxides of elements of Groups 1 or 11 of the Periodic Table
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/02Natural fibres, other than mineral fibres
    • D06M2101/04Vegetal fibres
    • D06M2101/06Vegetal fibres cellulosic
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/30Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/32Polyesters

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Treatment Of Fiber Materials (AREA)

Abstract

Present invention is disclosed a kind of step fiber opening method of polyester-nylon composite superfine fibre two, including S1, Alkali reduction fibrillation step:On the two big rubbing surface guide wheel that polyester-nylon composite superfine fibre cloth is sleeved on to liquid stream dye machine, in the first fibrillation liquid and auxiliary agent, with the first fibrillation temperature, water slug tests and guide wheel rotating speed are specified, the fibrillation rate for making polyester-nylon composite superfine fibre cloth by the fibrillation of the very first time reaches first predetermined value;S2, mechanical fibrillation step:By the polyester-nylon composite superfine fibre cloth Jing Guo Alkali reduction fibrillation on the big rubbing surface guide wheel that liquid stream contaminates machine, in the second fibrillation liquid and auxiliary agent, with the second fibrillation temperature, water impact speed, water temperature and guide wheel rotating speed are specified, polyester-nylon composite superfine fibre cloth fibrillation rate after the mechanical fibrillation of the second time is reached second predetermined value.The beneficial effects of the invention are as follows using chemistry and mechanical secondary fibrillation method, influence of the chemical agent to fiber physical property can be not only reduced, and its Alkali reduction can be controlled in a relatively low scope.

Description

A kind of step fiber opening method of polyester-nylon composite superfine fibre two
Technical field
The present invention relates to a kind of fiber opening method, more particularly to a kind of step fiber opening method of polyester-nylon composite superfine fibre two.
Background technology
It is a kind of composite fibre produced by composite spinning technology to wash brocade compound, and polyester-nylon complex fiber passes through fibrillation Turn into superfine fibre after processing.
And be as the most basic requirement of automatic assembly line spool cloth (polyester-nylon composite superfine fibre cloth):Fibrillation is fully (logical Normal polyester-nylon composite superfine fibre fibrillation rate is just believed that fibrillation meets the requirements when reaching 60%);Meanwhile, to have enough strength and The winding resilience of thickness and fabric, flat deflection reaches most preferably, to ensure that cloth cover long-time stable on automatic erasing line is transported Turn.
However, the fibrillation of existing polyester-nylon complex fiber is realized often through chemical fiber opening method, and chemical fiber opening method It is divided into acidic treatment, alkali process method and organic solvent method again, and polyester-nylon composite superfine fibre is in the processing of Alkali reduction fibrillation, one As all use alkali decrement method, i.e., polyester-nylon composite superfine fibre is arranged in fibrillation liquid, make to wash bright and beautiful bicomponent filament yarn fibrillation liquid, Hydrolyzed under temperature, time and the comprehensive function of accelerator, terylene and polyamide fibre are cracked into single superfine fibre.
Meanwhile, it is continuously increased with the concentration, temperature, time of caustic soda, fibrillation is more and more abundant, the fiber number of superfine fibre Attenuate, monofilament increasing number, fabric thickness first increases, soft, water absorption, suction solvent borne, dirt-removing power, wiping effect are equal Reach optimum state.
But fibrillation is bigger, Alkali reduction is also bigger, and superfine fibre constantly occurs to hydrolyze and constantly attenuate, therefore strength of filament Diminish, fiber stiffness (fibrous fracture intensity) declines, fabric thickness and grammes per square metre also decline therewith, cause fabric construction loose, knit The winding resilience of thing and flat deflection decline, and strength also declines therewith, easily slippage and lose use value, it is impossible to realize fibrillation The active balance of abundant and fabric intensity and thickness.
The content of the invention
The purpose of the present invention is exactly to pass through chemical technology there is provided one kind to solve the above-mentioned problems in the prior art The mode combined with mechanical technology ensures fibrillation fully and fabric has the polyester-nylon composite superfine fibre of enough intensity and thickness Fiber opening method.
The purpose of the present invention is achieved through the following technical solutions:
A kind of step fiber opening method of polyester-nylon composite superfine fibre two, comprises the following steps:
S1, Alkali reduction fibrillation step:The two big rubbing surface that polyester-nylon composite superfine fibre cloth is sleeved on into liquid stream dye machine is led On wheel, in the first fibrillation liquid and auxiliary agent, with the first fibrillation temperature, water slug tests and guide wheel rotating speed are specified, by the very first time Fibrillation the fibrillation rate of polyester-nylon composite superfine fibre cloth is reached first predetermined value;
S2, mechanical fibrillation step:The polyester-nylon composite superfine fibre cloth Jing Guo Alkali reduction fibrillation is contaminated into the big of machine in liquid stream to rub On the guide wheel of wiping face, in the second fibrillation liquid and auxiliary agent, with the second fibrillation temperature, water impact speed, water temperature and guide wheel is specified to turn Speed, makes polyester-nylon composite superfine fibre cloth fibrillation rate after the mechanical fibrillation of the second time reach second predetermined value.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:Two big rubbing surfaces are led Wheel has difference in height, and they include gap in rotating shaft, the rotating shaft and are provided with two pieces of baffle plates coaxial with the rotating shaft, institute The column casing for being provided with that the section that 4-8 block web plates enclose is regular polygon between baffle plate is stated, the column casing is enclosed with the baffle plate Into stopper slot.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The first fibrillation liquid includes The concentration of sodium hydroxide, wherein sodium hydroxide is 6-8g/L.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The auxiliary agent is comprehensive effect refining Consumption in agent, and Alkali reduction fibrillation step is more than the consumption in mechanical fibrillation step.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:S1, Alkali reduction fibrillation step In bath raio be 1:10.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The first fibrillation temperature is 90~115 degrees Celsius;The water slug tests are 0.15-0.25MPA;The guide wheel rotating speed is 10HZ.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The first fibrillation temperature is 90~95 degrees Celsius, the specified water slug tests are 0.2MPA.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The very first time is 55- 65min。
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The first predetermined value is 38-42%.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The group of the second fibrillation liquid Divide same with the first fibrillation liquid phase, wherein the concentration of sodium hydroxide is 0.1-0.9g/L.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The water impact speed is 35HZ, the water temperature is 90~115 degrees Celsius, and the second fibrillation temperature is 100~115 degrees Celsius.
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:Second time is 110- 130min。
It is preferred that, a kind of described step fiber opening method of polyester-nylon composite superfine fibre two, wherein:The second predetermined value is 70%-80%.
The advantage of technical solution of the present invention is mainly reflected in:
1. deft design of the present invention, the usual think of for changing traditional fiber opening process often through chemical fibrillation to realize Dimension, by effective combination of chemical fibrillation and mechanical fibrillation, on the basis of it ensure that fibrillation adequacy, turn avoid single super Fine fibre because hydrolyze it is meticulous there is the problem of fibrous fracture intensity declines, it is ensured that fabric have sufficient intensity, thickness and Resilience is wound, realize fibrillation fully has abundant intensity, thickness and wind elastic active balance with fabric.
2. the present invention's is simple to operate, each step linking is close, by the control to fibrillation rate and to Guiding wheel structure Improve, the frictional force between increase polyester-nylon composite superfine fibre cloth and guide wheel contact surface, so as to provide necessity for mechanical fibrillation Condition;And after mechanical fibrillation, it is possible to reduce individually using the amount of the fibrillation liquid required for chemical fibrillation, be conducive to drop The production cost of low enterprise.
Brief description of the drawings
Fig. 1 is the common Guiding wheel structure schematic diagram of prior art;
Fig. 2 is big rubbing surface guide wheel schematic diagram in the present invention.
Embodiment
The purpose of the present invention, advantage and feature, will be carried out by the non-limitative illustration of preferred embodiment below diagram and Explain.These embodiments are only the prominent examples using technical solution of the present invention, it is all take equivalent substitution or equivalent transformation and The technical scheme of formation, all falls within the scope of protection of present invention.
The step fiber opening method of a kind of polyester-nylon composite superfine fibre two that the present invention is disclosed, using first Alkali reduction fibrillation (chemical work Skill), the two-step method of rear machinery fibrillation changes the general usual thinking that fibrillation is carried out only with chemical technology of traditional handicraft.
Specifically, this method comprises the following steps:
S1, Alkali reduction fibrillation step:The polyester-nylon composite superfine fibre cloth of specified wt is sleeved on to two on liquid stream dye machine On the individual big rubbing surface guide wheel 1 with difference in height, the first fibrillation liquid and auxiliary agent of specified wt are added in liquid stream dye machine, and is made Bath raio in Alkali reduction fibrillation step is 1:10.
Wherein, the first fibrillation liquid includes sodium hydroxide, and the sodium hydroxide is 100% piece alkali, and every liter molten The quality of sodium hydroxide is 6-8g in liquid, more preferably 7-8g;The auxiliary agent is comprehensive effect refining agent.
Then, the temperature in the liquid stream dye machine is adjusted to the first fibrillation temperature, the first fibrillation temperature is 90~115 Degree Celsius, preferably 95 degrees Celsius.
Then, start the liquid stream dye machine, make the big rubbing surface guide wheel 1 with the first guide wheel rotational speed, it is described to rub greatly The rotating speed of wiping face guide wheel 1 is 10HZ, and two big rubbing surface guide wheels 1, which are rotated, drives the polyester-nylon composite superfine fibre cloth as belt The circulating rolling equally in the first fibrillation liquid, now, occurs water between polyester-nylon composite superfine fibre macromolecule and the first fibrillation liquid Solution reaction, ultimately forms water-soluble substances.
Specifically, in the first fibrillation liquid, the ester linkage hydrolyzing fracture of the macromolecular chain on superfine fibre surface is constantly formed not With the hydrolysate of the degree of polymerization, meanwhile, the comprehensive effect refining agent is adsorbed on the superfine fibre surface rapidly, reduces fiber table The tension force in face, secondly, ion exchange occurs for hydroxyl radical negative ion in the anion and the first fibrillation liquid in the comprehensive effect refining agent Reaction, hydroxide ion shifts and is enriched in superfine fibre surface, is that hydroxide ion has the also attack more easily of more chances Carbon atom with part positive charge in superfine fibre macromolecule, makes superfine fibre high score quantum splitting, so that promote hydrolysis, Ultimately form water miscible phthalic acid sodium and ethylene glycol.
With the continuous progress of hydrolysis so that the fiber number (diameter) of superfine fibre attenuates, and monofilament increases, brocade is washed compound The weight of superfine fibre cloth reduces, and Alkali reduction is incrementally increased.
Simultaneously also along with certain mechanical fibrillation process in Alkali reduction fibrillation step, but mechanical kinetic energy is auxiliary Reason, the main cause or sodium hydroxide and the hydrolysis of superfine fibre of fibrillation.
After the Alkali reduction fibrillation of the very first time is carried out, polyester-nylon composite superfine fibre fibrillation rate is set to reach first predetermined value, Stop the Alkali reduction fibrillation step.
But in above process, how controlling the stopping of Alkali reduction fibrillation process and starting mechanical fibrillation process is guarantee The present invention can realize the maximum difficult point of final result, and the experiment through inventor many times is found with long-term thinking analysis: In caustic reduction processing, before fibrillation rate reaches 40%, the Stiffness of superfine fibre is not obvious, and when fibrillation rate is more than 40% Afterwards, the rigidity of superfine fibre is decreased obviously;Therefore the present invention preferably first predetermined value is 38-42%;Further, it is excellent Elect as when reaching 40%, stop above-mentioned Alkali reduction fibrillation process, now, Alkali reduction is about 14%-15%;It is corresponding, to reach To above-mentioned fibrillation rate, corresponding Alkali reduction fibrillation process duration is about 55-65min, more preferably 60min.
S2, mechanical fibrillation step:Then, the polyester-nylon composite superfine fibre cloth Jing Guo Alkali reduction fibrillation is stilled remain in into institute On the big rubbing surface guide wheel 1 for stating liquid stream dye machine.
The first fibrillation liquid is discharged from the liquid stream dye machine, and the second fibrillation liquid is added in the liquid stream dye machine And auxiliary agent, and the bath raio in mechanical fibrillation step is maintained at 1:120.
Wherein, the component and auxiliary agent of the second fibrillation liquid and the component and auxiliary agent of the first fibrillation liquid are identical, But the concentration of sodium hydroxide will be far smaller than the naoh concentration in the first fibrillation liquid in wherein described second fibrillation liquid, The quality of sodium hydroxide is 0.1-0.9g, and use of the auxiliary agent in mechanical fibrillation step in specially every liter the second fibrillation liquid Amount is less than the consumption in the Alkali reduction fibrillation step.
Because mainly being realized in Alkali reduction fibrillation step by the hydrolysis of sodium hydroxide and superfine fibre Fibrillation, and mechanical kinetic energy is then relied primarily in mechanical fibrillation step and carries out fibrillation, the second fibrillation liquid and auxiliary agent mainly play auxiliary Effect.
Then, the temperature in liquid stream dye machine is adjusted to the second fibrillation temperature, the second fibrillation temperature is 100~115 Degree Celsius, due to fibrillation temperature and fibrillation speed holding direct ratio, temperature is higher, and fibrillation effect is better, and temperature is reduced, then fibrillation Speed is reduced, and therefore, why the second fibrillation temperature setting is slightly over into the first fibrillation temperature, is in order to anti-in no chemistry On the premise of answering, the speed of acceleration mechanical fibrillation.
Then, described to wash brocade compound super to specify water impact speed to be sprayed at the water of assigned temperature for control water spraying mechanism Thin fiber cloth and the region of guide wheel contact;The water impact speed is 35HZ, and the water temperature is 90~115 degrees Celsius.
Start the liquid stream dye machine, make the big rubbing surface guide wheel 1 to specify rotational speed, the big rubbing surface guide wheel 1 Rotating speed is 10HZ, and the big rubbing surface guide wheel 1, which is rotated, drives the polyester-nylon composite superfine fibre cloth to be circulated in the second fibrillation liquid Roll, by the second time and make polyester-nylon composite superfine fibre fibrillation rate reach second predetermined value stop, second time Preferably 110-130min, more preferably 120min.
In mechanical fibrillation step, because the content of sodium hydroxide in the second fibrillation liquid is with respect to hydroxide in the first fibrillation liquid The content of sodium greatly reduces, and concentration is substantially reduced, now, between the polyester-nylon composite superfine fibre cloth and sodium hydroxide hardly Generation hydrolysis, therefore, the diameter of single superfine fibre no longer reduce substantially, Alkali reduction also substantially with the Alkali reduction fibrillation Alkali reduction in step is consistent, and is at this moment mainly led by the polyester-nylon composite superfine fibre cloth with two big rubbing surfaces The mechanical energy such as frictional force, the impulsive force of current and the polyester-nylon composite superfine fibre cloth contractility of itself between wheel 1 realize into One step fibrillation.
However, inventor by test of many times find, if it is existing as shown in Figure 1 include the guide wheel of polyester roller Upper progress continuation fibrillation, the fabric of final production is unable to reach preferable fibrillation requirement at all, and therefore, inventor is further to institute Two guide wheels for stating liquid stream dye machine are improved.
Specifically, as shown in Figure 2, two big rubbing surface guide wheels 1 include gap in rotating shaft 11, the rotating shaft 11 It is provided between two pieces of circular baffle plates 12 coaxial with the rotating shaft 11, the baffle plate 12 to be provided with 4-8 blocks and enclose section and is Several through holes are offered on the web plate 13 of regular polygon, each half tone 13, preferably described web plate 13 is six pieces, and they enclose The hollow column casing of the synthesis regular hexagon that one coaxial with the rotating shaft 11 and section is, and the area of section of the column casing is small In the baffle plate 12, the outer wall of the column casing and two baffle plates 12 are together to form a stopper slot, described to wash during fibrillation Brocade composite superfine fibre cloth is stuck in the stopper slot.
In the detailed process of mechanical fibrillation, the polyester-nylon composite superfine fibre cloth is fitted on the surface of the column casing, Due to thering are 6 drift angles to withstand on the polyester-nylon composite superfine fibre cloth on the now column casing, and the surface of six blocks of web plates 13 with The polyester-nylon composite superfine fibre cloth is there is also contact, and therefore, their contact area is far longer than leading for existing polyester roller The contact area of wheel and the polyester-nylon composite superfine fibre cloth, so the guide wheel 1 after improving is to polyester-nylon composite superfine fibre charity Plus the relatively existing guide wheel of frictional force also greatly increase, so as to add the power of polyester-nylon composite superfine fibre cloth fibrillation, make Obtain polyester-nylon composite superfine fibre cloth and can continue to fibrillation.
Simultaneously as when current spray to polyester-nylon composite superfine fibre cloth, one is applied to the polyester-nylon composite superfine fibre cloth Fixed impulsive force, on the one hand further increases the frictional force between the guide wheel and polyester-nylon composite superfine fibre cloth contact surface, increases The power of fibrillation is added;On the other hand, water impact also cause polyester-nylon composite superfine fibre cloth itself occur vibration, deformation and It is flexible, so as to further increase the power of polyester-nylon composite superfine fibre cloth fibrillation, also cause polyester-nylon composite superfine fibre cloth Wind resilience increase;Furthermore, due to being provided with some through holes on the web plate 13, therefore under the impact of current, wash brocade multiple Closing the different piece of superfine fibre cloth can respectively be deformed and be absorbed in the through hole, many places by reference of different through holes The winding resilience for also further increasing polyester-nylon composite superfine fibre cloth occurs while deformation.
By mechanical fibrillation step, can on the basis of first time fibrillation fibrillation 30%-40% again so that final production The fibrillation rate of product is that the second predetermined value reaches 70%-80%, meets the fibrillation requirement of final fabric.
Further, after using mechanical fibrillation, the further hydrolysis of single superfine fibre can be effectively prevented, so as to keep away Exempt from the diameter reduction of single superfine fibre to the obvious undesirable situation of fibrous fracture intensity, after this method, finally The Alkali reduction of fabric maintains 14%-15%, and caustic reduction processing production is far smaller than used alone and meets the requirement of fibrillation rate Alkali reduction (about 20%) corresponding to fabric, therefore the thickness of final fabric also will with respect to the fabric that caustic reduction processing is used alone Thickness, it is achieved thereby that the active balance of above-mentioned multi-effect.
The present invention still has numerous embodiments, all technical sides formed by all use equivalents or equivalent transformation Case, is within the scope of the present invention.

Claims (8)

1. a kind of step fiber opening method of polyester-nylon composite superfine fibre two, it is characterised in that:Comprise the following steps:
S1, Alkali reduction fibrillation step:On the two big rubbing surface guide wheel that polyester-nylon composite superfine fibre cloth is sleeved on to liquid stream dye machine, In the first fibrillation liquid and auxiliary agent, with the first fibrillation temperature, water slug tests and guide wheel rotating speed are specified, by the fibrillation of the very first time The fibrillation rate of polyester-nylon composite superfine fibre cloth is set to reach first predetermined value;
S2, mechanical fibrillation step:Polyester-nylon composite superfine fibre cloth Jing Guo Alkali reduction fibrillation is contaminated to the big rubbing surface of machine in liquid stream On guide wheel, in the second fibrillation liquid and auxiliary agent, with the second fibrillation temperature, water impact speed, water temperature and guide wheel rotating speed are specified, is made Polyester-nylon composite superfine fibre cloth fibrillation rate after the mechanical fibrillation of the second time reaches second predetermined value;
Two big rubbing surface guide wheels(1)With difference in height, and they include rotating shaft(11), the rotating shaft(11)Upper gap It is provided with two pieces and the rotating shaft(11)Coaxial baffle plate(12), the baffle plate(12)Between be provided with 4-8 block web plates(13)Enclose The section of synthesis is the column casing of regular polygon, the column casing and the baffle plate(12)Enclose stopper slot;
The very first time is 55-65min, and the first predetermined value is 40%;The first fibrillation liquid includes sodium hydroxide, its The concentration of middle sodium hydroxide is 6-8g/L;The component of the second fibrillation liquid is same with the first fibrillation liquid phase, wherein hydroxide The concentration of sodium is 0 .1-0 .9g/L.
2. the step fiber opening method of a kind of polyester-nylon composite superfine fibre two according to claim 1, it is characterised in that:The auxiliary agent It is the consumption that consumption in comprehensive effect refining agent, and Alkali reduction fibrillation step is more than in mechanical fibrillation step.
3. the step fiber opening method of a kind of polyester-nylon composite superfine fibre two according to claim 2, it is characterised in that:S1, alkali subtracts It is 1 to measure the bath raio in fibrillation step:10.
4. the step fiber opening method of a kind of polyester-nylon composite superfine fibre two according to claim 3, it is characterised in that:Described first Fibrillation temperature is 90 ~ 115 degrees Celsius;The water slug tests are 0 .15-0 .25 MPa;The guide wheel rotating speed is 10Hz.
5. the step fiber opening method of a kind of polyester-nylon composite superfine fibre two according to claim 4, it is characterised in that:Described first Fibrillation temperature is 90 ~ 95 degrees Celsius, and the specified water slug tests are 0 .2MPa.
6. the step fiber opening method of a kind of polyester-nylon composite superfine fibre two according to claim 1, it is characterised in that:The current Impact velocity is 35Hz, and the water temperature is 90 ~ 115 degrees Celsius, and the second fibrillation temperature is 100 ~ 115 degrees Celsius.
7. the step fiber opening method of a kind of polyester-nylon composite superfine fibre two according to claim 6, it is characterised in that:Described second Time is 110-130min.
8. the step fiber opening method of a kind of polyester-nylon composite superfine fibre two according to claim 7, it is characterised in that:Described second Predetermined value is 70%-80%.
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* Cited by examiner, † Cited by third party
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006014077A1 (en) * 2004-08-04 2006-02-09 Sunghoon Choi A method for dyeing microfibers and fabric woven with microfibers dyed thereby
EP2011917A2 (en) * 2007-07-05 2009-01-07 Formosa Taffeta Co.,Ltd. Method for manufacturing embossed conductive cloth
CN201546050U (en) * 2009-06-03 2010-08-11 台嘉玻璃纤维有限公司 High-pressure fiber opening device
CN103541213A (en) * 2013-09-11 2014-01-29 盛虹集团有限公司 Dyeing and finishing process for polyester brocade sydney down cotton-imitated fabric
CN203498636U (en) * 2013-10-16 2014-03-26 陕西宝昱科技工业有限公司 High-pressure water fiber splitting device

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH073638A (en) * 1993-06-17 1995-01-06 Toyobo Co Ltd Production of splittable conjugate fiber woven fabric
JP5715741B1 (en) * 2014-03-13 2015-05-13 西川勝彦 Structure containing split fiber type composite fiber and method for producing the same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006014077A1 (en) * 2004-08-04 2006-02-09 Sunghoon Choi A method for dyeing microfibers and fabric woven with microfibers dyed thereby
EP2011917A2 (en) * 2007-07-05 2009-01-07 Formosa Taffeta Co.,Ltd. Method for manufacturing embossed conductive cloth
CN201546050U (en) * 2009-06-03 2010-08-11 台嘉玻璃纤维有限公司 High-pressure fiber opening device
CN103541213A (en) * 2013-09-11 2014-01-29 盛虹集团有限公司 Dyeing and finishing process for polyester brocade sydney down cotton-imitated fabric
CN203498636U (en) * 2013-10-16 2014-03-26 陕西宝昱科技工业有限公司 High-pressure water fiber splitting device

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
涤/锦复合超细纤维织物的开纤效果与服用舒适性;沈淦清 等;《北京服装学院学报》;19880430;第18卷(第1期);第27-29页第1节和第2.1节 *
涤锦复合超细纤维开纤工艺的制定;李志群 等;《印染技术》;20101231(第6期);第39页第2.4节、第40页图1(c)和图2(c)以及第4.1节 *

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