CN1648293A - High whiteness viscose staple fiber for health material and its producing process - Google Patents
High whiteness viscose staple fiber for health material and its producing process Download PDFInfo
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Abstract
The present invention relates to high whiteness viscose staple fiber for health material and its production process, and belongs to the field of non-woven fabric technology. The viscose staple fiber product has whiteness higher than 87 %, and is produced with the material including cellulose fiber 86.7-92 wt%, water 7.8-13 wt% and oil preparation 0.08-0.30 wt%. The production process includes: soaking material in alkali solution at 50 deg.c; squeezing and crushing in squeezer; maturing at 49-51 deg.c; yellowing with carbon disulfide at 17-35.5 deg.c for 24-28 min; acid bathing at 48-49 deg.c for 1.8-2.0 sec; drafting and collecting; secondary bleaching with sodium hypochlorite and hydrogen peroxide; stoving in stove; fining opening and packing. The present invention has excellent hygroscopicty, permeability, comfort, no toxicity and no corrosion, and is suitable for producing non-woven fabric used in medical field.
Description
Technical field
The present invention relates to a kind of raw material viscose staple fibre and production method of non-weaving cloth industry, particularly relate to a kind of high whiteness viscose staple fiber for health material and production technology thereof.
Background technology
About so far 100 years history of common viscose staple fibre development, its quality index requires and the method for inspection is seen GB/T14463-1993 " viscose staple fibre " standard.Because its quality index determines it can only be mainly used in the traditional textile spinning.12 of its quality index, intensity, whiteness are lower, and cleanliness factor is poor, and contains trace toxic material sulphur, chlorine, can not be used for disposable medicine, hygienic material.Traditional medicine hygienic material raw material mainly is a natural cotton.The natural cotton resource-constrained needs a few procedure removal of impurities, purification, bleaching, degreasing etc., just can be used for producing, and has limited the large-scale production development of disposable sanitary articles greatly, has limited fast-developing in recent years non-woven sanitary articles for use industry.
Summary of the invention
It is main raw material with the cellulose fibre that purpose one of the present invention provides a kind of, cleanliness factor height, hygienic environment-protecting, suitable pharmaceutical sector is used defends material with high whiteness glue staple fibre, two to provide a kind of technological process simple, scientific and reasonable, the production technology of the high whiteness glue staple fibre that the production precision is high overcomes the many deficiencies in the background technology.
The technical scheme that realizes the foregoing invention purpose is: the whiteness of this product greater than 87%, residual sulfur content is low, intensity is high, degree of stretching height, oil content is low, cleanliness factor is high, surface-active substance is low, the hydrotrope is low, the oven dry xanthochromia is little, pH value is neutral, water absorption is big, absorbent time short (speed is fast), certain curling, asepsis environment-protecting is arranged, other index meets the GB high-class product.The raw material and the weight percent content of this product are: cellulose fibre 86.7-92%, water 7.8-13%, finish 0.08-0.30%.
A kind of production technology of making high whiteness viscose staple fiber for health material, it comprises the following steps
A, dipping: raw material is put into temperature: 50 ℃, time: 31-33 minute, the concentration of alkali: 220g/L: V-388 consumption: 0.05-0.06% (first fibre)
B, squeezing: raw material is pulverized the heavy 130-140 grams per liter of constant volume with the squeezer squeezing;
C, experienced: the raw material after will pulverizing is experienced, and temperature 49-51 ℃, experienced outlet copper is sticking to be 48mp;
D, yellow: carbon disulfide is to the fine addition 33-34% of first, and the yellow time is 24-28 minute, temperature 17-35.5 ℃;
E, spinning:
Acid bath: use the acid solution acid bath, sulfuric acid concentration: 110-115g/L, sodium sulfate concentration: 335-355g/L, zinc sulfate concentration: 10.5-11.5g/L, acid bath temperature: 48-49 ℃, acid bath drop :≤6g/L, the acid bath time is 1.8-2.0 second;
Two bathe: temperature 〉=92 ℃, and sulfuric acid concentration: 50-60g/L, sodium sulfate concentration: 115-125g/L, two bath times were 10-19 second;
F, drawing-off, boundling
Continuous twice drawing-off is adopted in the plasticizing drawing-off, high draft of the first road drawing-off, degree of draft is 65-68%, improve cellulose macromolecule crystalline orientation degree, make it have high strength flatness degree, the retraction drawing-off of second road, degree of draft is-1%-0.8%, under the situation of damage strength, carry high ductility and improve fragility slightly, and make it have certain curling; Finally make fiber have good serviceability by the secondary drawing-off.
Total draft: 2.13-2.18 times, spinneret draft: 1.28-1.32 doubly;
G, concise:
99 ℃ of fine hair groove boiling temperatures, pickling temperature 〉=80 ℃, 80 ℃ of washings, 80-85 ℃ of desulfurization bath temperature, desulfurization alkali concn 2.5g/L, 70 ℃ of two washing temperature, concise time: 11-13 minute;
H, carry out secondary bleaching with clorox, hydrogen peroxide, first step sodium hypochlorite bleaching is arranged in bleachery, clorox concentration 0.5-1.2g/L, 60 ℃ of temperature, pH value 9.5,70 ℃ of three or four washing temperature, three washing pH value 5.0-6.0,70 ℃ of oil bath concentration 3g/L, temperature, the second step hydrogen peroxide bleaching is arranged in the workshop section that oils, hydrogen peroxide concentration 0.6-1.0g/L, 70 ℃ of temperature, pH value 7.0;
I, oven dry: Tumble Dry, bake out temperature is 60-130 ℃, after the oven dry, with the smart shredding of finished product, packing.
Owing to adopted technique scheme, the present invention is main matter with the cellulose fibre, can save a large amount of cottons, its remarkable advantage is, this product is different with common viscose staple fibre performance indications, common viscose staple fibre is pressed the GB/T14463-1993 standard, and totally 12 of quality index mainly are suitable for the cotton spinning industry.This product except that common 12 quality index, at non-woven with the newly-increased again outward appearance of raw material, wetly stretch, crispation number, crimpness, xanthochromia, the hydrotrope, surface-active substance, stain impurity, water absorption, water imbibition, finished acid basicity amount to 10 quality index.With reference to the up-to-date method of inspection of domestic, international non-woven industry, formulate the method for inspection of these 10 projects.This method of inspection gets the nod international and domestic colleague.Compare with mill run, every index surpasses common viscose staple fibre.Product of the present invention belongs to environmental protection fiber, not only have good hygroscopicity, gas permeability, comfortable and easy to wear, extremely low because of its whiteness height, cleanliness factor height, sulfur content, do not contain organochlorine, characteristics such as nontoxic, no burn into soda acid neutrality meet directly textiles requirement of wearing clothes next to the shin, are suitable for being directly used in the manufacturing nonwoven, be applied to medical treatment, health field, nonwoven disposable material products such as processing baby diaper, hospital gauze, bandage.Having solved traditional medicine hygienic material raw materials for production mainly is the resource-constrained present situation of natural cotton, and for the non-woven material industry of defending provides abundant raw material, making makes rational use of resources provides a new way.Promote the large-scale production development of disposable sanitary articles.When this launch products obtains extensive favorable comment, caused the great interest of international customers such as Japan, Italy, Korea S, success has exported to states such as the U.S., Switzerland, Italy, Turkey in a large number.Along with improving constantly of people's living standard, the demand of this environment-friendly type textile raw material constantly increases, and market is widely at home and abroad arranged, and supply falls short of demand, belongs to high value added product, and quality requirement is strict.
The specific embodiment
A, products material embodiment
Cellulose fibre is a main matter of the present invention, and its raw material components and percentage by weight are: cellulose fibre 86.85-92%, water 7.8-13%, finish 0.08-0.30%.
Raw material components and weight percent content embodiment:
1, cellulose fibre 86.85, water 13, finish 0.15..
2, cellulose fibre 92, water 7.92, finish 0.08..
3, cellulose fibre 91.9, water 7.80, finish 0.30..
4, cellulose fibre 86.7, water 13, finish 0.30.
5, cellulose fibre 88, water 11.8, finish 0.20.
The effect of three kinds of raw materials is:
Water, fiber are placed the nature moisture regain naturally, impossible over dry, and fiber product contains certain water when being produced can be antistatic.
Finish, lubricated, antistatic property have been processed in weaving, and make fiber have certain friction, and the fortifying fibre spinnability is easy to processing.
B, production technology embodiment
1, the capital equipment of Cai Yonging (seeing the following form)
| Sequence number | Title | Model | Country origin |
| 1 | Squeezer | AB72″ | Austria Lenzing company |
| 2 | Xanthating machine | SUMA27 | Austria Lenzing company |
| 3 | The viscose filtration machine | KKF18 | Austria Lenzing company |
| 4 | Spinning machine | SM80/800 | Austria Lenzing company |
| 5 | Refiner | Austria Lenzing company | |
| 6 | Dryer | U.S. PROCTOR company | |
| 7 | 11 imitate flash distillation | Germany Ebner company | |
| 8 | 4 grades of crystallizers | Germany Ebner company |
2., technological process
The present invention adopts the technological process in the technical scheme to be: feed the dregs of rice, dipping, squeezing, pulverize, experienced, fine cooling of alkali and conveying, yellow, dissolving, filter, maturation, deaeration, filter, spinning, two bathe, one drawing-off, two drawing-offs, three roller boundlings, cut off, concise (fine hair groove boiling, sour water is washed, one washing, desulfurization, two washings, a multiple tracks bleaching and pH value regulation and control, three washings and pH value regulation and control, four washings, oil bath and the bleaching of secondary multiple tracks and pH value regulation and control, three washings and pH value regulation and control, four washings, oil bath and the bleaching of secondary multiple tracks), oven dry (wet shredding, the oven dry of A section, middle shredding, the oven dry of B section, do shredding), smart shredding, packing.
Concrete technology:
Comprise the following steps
A, dipping: raw material is put into temperature: 50 ℃, time: 31-33 minute, the concentration of alkali: 220g/L: V-388 consumption: 0.05%-0.06% (first fibre)
B, squeezing: raw material is pulverized the heavy 130-140 grams per liter of constant volume with the squeezer squeezing;
C, experienced: sticking with experienced outlet copper, the raw material after pulverizing is experienced, and temperature 49-51 ℃, viscosity is 48mp;
D,, yellow: carbon disulfide is to the fine addition 33-34% of first, and the yellow time is 24-28 minute, temperature 17-35.5 ℃;
E, spinning:
Acid bath: use the acid solution acid bath, sulfuric acid concentration: 112g/L, sodium sulfate concentration: 345g/L, zinc sulfate concentration: 11g/L, the acid bath temperature: 49 ℃, acid bath drop: 6g/L, the acid bath time is 1.9 seconds;
Two bathe: temperature 〉=92 ℃, and sulfuric acid concentration: 55g/L, sodium sulfate concentration: 120g/L, two bath times were 10-19 second;
E, drawing-off, boundling
Continuous twice drawing-off is adopted in the plasticizing drawing-off, high draft of the first road drawing-off, and degree of draft is 65-68%, the retraction drawing-off of second road, degree of draft is-1%-0.8%;
Total draft: 2.13-2.18 times, spinneret draft: 1.28-1.32 doubly;
F, concise:
Fine hair groove boiling temperature 〉=98 ℃, pickling temperature 〉=80 ℃, 80 ℃ of washings, 80-85 ℃ of desulfurization bath temperature, desulfurization alkali concn 2.5g/L, 70 ℃ of two washing temperature, concise time: 12 minutes;
G, carry out secondary bleaching with clorox, hydrogen peroxide, first step sodium hypochlorite bleaching is arranged in bleachery, clorox concentration 0.5-1.2g/L, 60 ℃ of temperature, pH value 9.5,70 ℃ of three or four washing temperature, three washing pH value 5.0-6.0,70 ℃ of oil bath concentration 3g/L, temperature, the second step hydrogen peroxide bleaching is arranged in the workshop section that oils, hydrogen peroxide concentration 0.6-1.0g/L, 70 ℃ of temperature, pH value 7.0;
H, oven dry: Tumble Dry, bake out temperature is 60-130 ℃, after the oven dry, with the smart shredding of finished product, packing.
3. main technologic parameters
| The technology title | Unit | Numerical value | Control accuracy |
| The maceration extract temperature | ℃ | 49-51 | |
| Impregnation concentration | g/l | 220 | ±1 |
| V-388 consumption (to the first fibre) | ％ | 0.05-0.06 | |
| Alkali is fine to be formed: the fine alkali of first | ％ ％ | 31 16 | ±1 ±1 |
| Experienced outlet copper is sticking | mp | 55 | ±5 |
| CS2 addition (to the first fibre) | ％ | 33-34 | |
| Spinning glue is formed: the fine alkali of first | ％ ％ | 8.9 5.0 | ±0.1 ±0.1 |
| The spinning adhesiveness | S | 55 | ±7 |
| Spinning glue degree of ripeness | H | 16 | ±1.5 |
| Two bathe: the sulfuric acid concentration temperature | g/l ℃ | 40-50 ≥92 | |
| I road degree of draft | ％ | 65-68 | |
| II road degree of draft | ％ | -1-0.8 | |
| Fine hair forming tank temperature | ℃ | ≥98 | |
| Desulfurization is bathed: the NaOH temperature | g/l ℃ | 2-3 80-85 | |
| Bleaching bath: NaClO concentration-temperature pH value | g/l ℃ | 06-1.0 60 9.5 | ±0.5 |
| Oil bath: oil concentration H 2O 2Concentration-temperature | g/l g/l ℃ | 3-4 0.6-1.0 70 |
| PH value | 7.0 | ±0.5 | |
| Bao Chong | Kg | 220 | ±10 |
| Acid bath is formed: sulfate sulfatase sodium zinc sulfate | g/l g/l g/l | 113 345 11.0 | ±2 ±10 ±0.3 |
| The acid bath temperature | ℃ | 49 | ±1 |
4. key problem in technology
Compare with common viscose staple fibre and to have special technology and quality requirement, we have taked following concrete measure:
1, this product is used for non-weave non-woven fabrics, because of its processing mode decision finished product tearing strength, for improving the intensity of nonwoven fabric finished product, requires raw material intensity height and has certain curling.The present invention is for improving intensity, in many ways improve from production technology, improve the fine content of spinning glue first and bring up to 8.9% from 8.5%, the raising yellow adds the carbon amount and delays viscose ripening to reduce spinning glue degree of ripeness, improve spinning glue and contain alkali, reduce the spinning bath sulfuric acid concentration, delay fiberizing, improve fiberizing by above-mentioned measure, cooperate and improve spinning one degree of draft, the drawing-off of reduction shower nozzle, make fibre strength improve 15%-25% than mill run.Reduce the spinning bath sulfuric acid concentration simultaneously,, make fiber have certain curling, help non-woven water thorn and produce, thereby improve fiber quality and spinnability greatly by above-mentioned measure.
2, this fibre whiteness requires more than 87%, the original sodium hypochlorite bleaching technology that adopts of my company, whiteness can only maintain between the 82-84%, just might improve the finished product whiteness so must carry out twice bleaching, because of bleaching for the second time can only be carried out in the workshop section that oils, and the bleaching back does not have washing, so select the hydrogen peroxide of nontoxic natural decomposition to make bleaching agent.By concentration, temperature, pH value, circular flow adjustment, the finished product whiteness has been reached more than 87%.When producing this fiber in addition, select to use the higher pulp raw material of whiteness, improve the whiteness of finished product.
3, this product is mainly used in medical treatment, health field, thereby, can not contain organochlorine in the finished product, so, the pulp of chlorine-free bleaching at first must be used from the raw material.This product adopts whole wood pulp production technology, use from Canada, the U.S., etc. the chlorine-free bleaching wood pulps of state's import.
4, the residual sulfur content of finished product requires below 8mg/100g.The residual sulphur of the mill run of my company is generally about 10-12mg/100g.For this reason, the present invention improves emphasis technology, at first adjusts fine hair forming tank temperature and brings up to more than 98 ℃ from original 96 ℃, makes the more abundant evaporation of fiber carbon disulfide (this operation makes the abundant shredding of fiber simultaneously, has increased curling of fiber).Four micropore acid bath filters have been increased, improve the acid bath filtration yield, important indicator-acid bath transparency the integral body that influences the residual sulphur of finished product has been improved about 20%, simultaneously, we increase by 15 millipore filters again and desulfurization bath, acid water, two are bathed all filter, and the desulphurization circulating amount hour is brought up to 1.4 cubes of/ton silks hour by 1.1 cubes of/ton silks.The 4-8mg/100g that controlled to the residual sulfur content success of this fiber.
5, pH value, surface-active substance technology controlling and process
These parameters is extremely important to the nonwoven production raw material, the defective product quality that influences of pH value; Whether the surface-active substance index meets the requirements is to a certain degree determining the hydro-entangled non-woven fabric production technology, and the defective hydro-entangled non-woven fabric production process chopping block equipment plug-hole that causes of this index has a strong impact on ordinary production.The pH value adjustment divides two parts, and a bleaching process adds the 20g/L dilute sulfuric acid and adjusts pH value to 9.5 in bleaching bath, and three washing steps transfer the oil bath pH value to 5.0-6.0 with adding the dilute sulfuric acid mode.Surface-active substance mainly divides two parts, reduces below the finished product oil content to 0.15%, and the addition of strict control viscose glue, acid bath auxiliary agent cooperates an amount of hot water wash to guarantee that above-mentioned two indexs are qualified at last.
6, xanthochromia, hydrotrope technology controlling and process
The adjustment of binomial index mainly relies on stable output, stable body lotion concentration, increase the drip washing groove by transforming again, guarantee the washing amount and the washing time of enough abilities, guarantee the washing (water yield, water quality, temperature) of fully necessary fresh soft water, wash the chemical industry materials such as unnecessary salt that the process fiber surface adheres to off, improve the health quality of fiber.
7, the particularity of special-purpose high its purposes of whiteness short rayon fiber denapon of nonwoven fabric has extremely strict requirement to the impurity contents such as stain in the finished product.In order to reduce the impurity content in the finished product, existing equipment a large amount of transformations have been carried out.Go into the place at former slop feeding and install capping additional, dryer is changed the novel seal bar, makes the postprocessing working procedures of product be in full closeding state, has stopped to leak the pollution of hair and outer bound pair fiber.Newly-increased millipore filter has been realized two baths, outward appearance: no color differnece, color spot, stain, dirt, peculiar smell, foreign matter
The stain foreign material: the stain of diameter 0.5-1.0mm is less than 10/2 kilograms products
Do fracture strength: 2.50CN/dtex
Wet breaking strength: 1.30CN/dtex
Dried elongation at break: 21.4%
Wet elongation at break: 18.1%
Line density deviation ratio :-0.60%
Length variation rate: 1.1%
Overcut fibre: 0.4%
Over-length fibre: 0.3mg/100g
Residual sulfur content: 7.5mg/100g
Fault: 1.2mg/100g
Greasy dirt yellowish fiber: 0mg/100g
Do the strong coefficient of variation: 8.90%
Whiteness: 89.3%
Crispation number: 3.82/cm
The rate of crispaturaing: 8.22%
Surface-active substance: less than 2mm
Finished acid basicity: neutrality
Hydrotrope content: 0.52%
Xanthochromia: qualified
Absorbent time: less than 10 seconds
Water absorption: greater than 15 gram/grams
Oil content: 0.10%
Regain: 10.87%
Grade: high-class product.
Outward appearance: no color differnece, color spot, stain, dirt, peculiar smell, foreign matter stain foreign material: the stain of diameter 0.5-1.0mm is less than 10/2 kilograms products
Do fracture strength: 2.50CN/dtex
Wet breaking strength: 1.30CN/dtex
Dried elongation at break: 21.4%
Wet elongation at break: 18.1%
Line density deviation ratio :-0.60%
Length variation rate: 1.1%
Overcut fibre: 0.4%
Over-length fibre: 0.3mg/100g
Residual sulfur content: 7.5mg/100g
Fault: 1.2mg/100g
Greasy dirt yellowish fiber: 0mg/100g
Do the strong coefficient of variation: 8.90%
Whiteness: 89.3%
Crispation number: 3.82/cm
The rate of crispaturaing: 8.22%
Surface-active substance: less than 2mm
Finished acid basicity: neutrality
Hydrotrope content: 0.52%
Xanthochromia: qualified
Absorbent time: less than 10 seconds
Water absorption: greater than 15 gram/grams
Oil content: 0.10%
Regain: 10.87%
Grade: high-class product.
Claims (2)
1, a kind of material of defending is characterized in that from spending viscose staple fibre its whiteness is greater than 87% with high, and its raw material and weight percent content are: cellulose fibre 86.7-92%, water 7.8-13%, finish 0.08-0.30%.
2, a kind of production technology of making claims 1 described high whiteness viscose staple fiber for health material is characterized in that it comprises the following steps
A, dipping: raw material is put into temperature: 50 ℃, time: 31-33 minute, the concentration of alkali: 220g/L, V-388 consumption: 0.05-0.06% (first fibre)
B, squeezing: raw material is pulverized the heavy 130-140 grams per liter of constant volume with the squeezer squeezing;
C, experienced: the raw material after will pulverizing is experienced, and temperature 49-51 ℃, experienced outlet copper is sticking to be 48mp;
D,, yellow: carbon disulfide is to the fine addition 33-34% of first, and the yellow time is 24-28 minute, temperature 17-35.5 ℃;
E, spinning bath:
Acid bath: use the acid solution acid bath, sulfuric acid concentration: 110-115g/L, sodium sulfate concentration: 335-355g/L, zinc sulfate concentration: 10.5-11.5g/L, acid bath temperature: 48-49 ℃, acid bath drop :≤6g/L, the acid bath time is 1.8-2.0 second;
Two bathe: temperature 〉=92 ℃, and sulfuric acid concentration: 50-60g/L, sodium sulfate concentration: 115-125g/L, two bath times were 10-19 second;
F, drawing-off, boundling
Continuous twice drawing-off is adopted in the plasticizing drawing-off, high draft of the first road drawing-off, and degree of draft is 65-68%, the retraction drawing-off of second road, degree of draft is-1%-0.8%;
Total draft: 2.13-2.18 times, spinneret draft: 1.28-1.32 doubly;
G, concise:
Fine hair groove boiling temperature 〉=98 ℃, pickling temperature 〉=80 ℃, 80 ℃ of washings, 80-85 ℃ of desulfurization bath temperature, desulfurization alkali concn 2.5g/L, 70 ℃ of two washing temperature, concise time: 11-13 minute;
H, carry out secondary bleaching with clorox, hydrogen peroxide, first step sodium hypochlorite bleaching is arranged in bleachery, clorox concentration 0.5-1.2g/L, 60 ℃ of temperature, pH value 9.5,70 ℃ of three or four washing temperature, three washing pH value 5.0-6.0, oil bath concentration 3g/L, temperature 70C, the second step hydrogen peroxide bleaching is arranged in the workshop section that oils, hydrogen peroxide concentration 0.6-1.0g/L, 70 ℃ of temperature, pH value 7.0;
The i oven dry: Tumble Dry, bake out temperature is 60-130 ℃, after the oven dry, with the smart shredding of finished product, packing.
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| CN101949080A (en) * | 2010-07-09 | 2011-01-19 | 江阴市华富纺织制衣有限公司 | Fabric containing gynostemma pentaphyllum fiber |
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| CN103290671A (en) * | 2013-06-17 | 2013-09-11 | 宜宾丝丽雅股份有限公司 | Refining and bleaching process of high-whiteness viscose staple fiber |
| CN103290671B (en) * | 2013-06-17 | 2015-07-01 | 宜宾丝丽雅股份有限公司 | Refining and bleaching process of high-whiteness viscose staple fiber |
| CN107794585A (en) * | 2016-08-25 | 2018-03-13 | 山东雅美科技有限公司 | A kind of preparation method of high white lustrous fibre cellulose fiber |
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| CN107794584A (en) * | 2016-08-25 | 2018-03-13 | 山东雅美科技有限公司 | The high white non-woven cloth regenerated celulose fibre of antibacterial and its production technology |
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| CN108547079B (en) * | 2018-06-08 | 2023-10-10 | 北京鹏盛天纤科技有限公司 | Green continuous production integrated device and process for absorbent cotton |
| CN110857350A (en) * | 2018-08-24 | 2020-03-03 | 松下电器产业株式会社 | Composite resin molded article |
| CN110857350B (en) * | 2018-08-24 | 2023-12-08 | 松下控股株式会社 | Composite resin molded article |
| US11891500B2 (en) | 2018-08-24 | 2024-02-06 | Panasonic Holdings Corporation | Composite resin molded article |
| CN110042489A (en) * | 2019-04-30 | 2019-07-23 | 阜宁澳洋科技有限责任公司 | A kind of preparation method of high crimp viscose |
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