CN103215824B - Application of dyeing auxiliary agent Univadine SD in high count high density polyester lining dyeing and finishing - Google Patents

Application of dyeing auxiliary agent Univadine SD in high count high density polyester lining dyeing and finishing Download PDF

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CN103215824B
CN103215824B CN201310079315.5A CN201310079315A CN103215824B CN 103215824 B CN103215824 B CN 103215824B CN 201310079315 A CN201310079315 A CN 201310079315A CN 103215824 B CN103215824 B CN 103215824B
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dyeing
univadine
count
polyester fabric
density polyester
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CN103215824A (en
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俞月莉
周强
姚建萍
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Shenghong Group Co Ltd
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Abstract

The invention discloses a method for manufacturing a high count high density polyester lining, which employs a refinement oil removing+dyeing+reduction cleaning one bath method, and selects a Huntsman Terasil SD type disperse dyestuff and a Univadine SD synthetic fibre refining-dyeing auxiliary combination for dyeing filament yarn fabric. The invention has the advantages of short technological process, low energy consumption, low dyeing sewage discharge and good dyeing color fastness, and accords with the development trend of printing and dyeing industry with wide application prospect and popularization potential.

Description

The application of dyeing assistant UNIVADINE SD in the dyeing and finishing of high-count and high-density polyester fabric
Technical field
The application relates to the application of dyeing assistant UNIVADINE SD in the dyeing and finishing of high-count and high-density polyester fabric.
Background technology
Since entering 21st century, China's textile industry obtains and develops rapidly, but simultaneously some problems also display gradually, as in short supply, the pollution etc. to ecological environment of the deficiency of natural resources, energy supply, constrain development speed and the scale of textile industry, and be on the rise.Economize energy and raw material, reduction consumption, change traditional developmental model, be take a new road to industrialization, the inevitable requirement of the strategy of sustainable development of implementing a scientific outlook on development, realize, be also the important measures incorporating globalised economy, strengthen enterprise competitiveness.
Dyeing is the industry of " high energy consumption, maximum discharge ".In dyeing process, electricity, coal, oil, vapour equal energy source consume high, account for more than 30% of processing cost, ten thousand yuan of output value comprehensive energy consumption average out tos, 0.86 ton of mark coal, 0.42 ton mark coal average than other industry exceeds more than one times, water consumption in dyeing process accounts for about 60% of whole textile industry water, and wastewater discharge is large, accounts for 60%-70% of printing and dyeing enterprise water consumption, being the 5th of national manufacturing enterprise total emission volumn, is the key industry that national energy-saving reduces discharging.The discharge of decreasing pollution thing, accomplishes cleaner production, contamination containment from source, be not only promote further textile industry industry restructuring, Economic Development Mode Conversion, also to protection of the environment, building a Harmonious Society is of great immediate significance.
At present, dyeing pre-treatment great majority adopt traditional alkali oxygen technique, in order to ensure product quality, generally adopt destarch, boiling-off technique and improve the pre-treatment processing method of liquid caustic soda, hydrogen peroxide and chemical assistant consumption, process route is long, chemical assistant consumption is large, energy consumption is high, quantity of wastewater effluent is large.
During tradition DISPERSE DYES high-temperature pressure dyeing, dye bath is generally carried out under mildly acidic conditions, this is because most of DISPERSE DYES dye-uptake under mild acid conditions is higher, coloured light is also more stable.If DISPERSE DYES dyes in alkaline bath, part DISPERSE DYES can be hydrolyzed, and some azo structure contained and DISPERSE DYES that is nitro structure is easily reduced.After these dyestuffs are hydrolyzed or reduce, its color and luster and dyefastness also all change.The Another reason causing dyestuff to decompose is that DISPERSE DYES has added a large amount of dispersant (NNO, sodium lignin sulfonate etc.) in the fabrication process, under 130 DEG C of high temperature, makes dye bath be alkalescence.Also because there is metal ion (Fe in dye bath +deng) under high-pressure steam, making the basic ions such as dye bath reduction and activity hydroxy, water-soluble increase, dye-uptake decline.
But DISPERSE DYES high-temperature pressure dyeing dyes and also there is a lot of weak point under mild acid conditions, particularly the appearance of superfine denier polyester fiber in recent years, makes it more to give prominence to.Such as: in (1) polyster fibre, there is the cyclic linear oligomer of less than 1.5%, in acid condition these oligomer to fiber surface transfer and with ca in hard water +, Mg +ions binding forms insoluble condensation product and sticks on fabric, and then under the effect of mechanical force, partial exfoliation, in dye bath, white powder occurs, and oligomer has certain affinity to dyestuff, can produce secondary aggregation and produce dye defect.(2) fabrics of polyester dyes under mild acid conditions, often makes leftover slurry and finish etc. bring dye bath into because pre-treatment is insufficient, and dyeing is produced, and look colored, look dirty phenomenon, affects the raising of dyeing quality.(3) because the concise and Alkali reduction of fabrics of polyester in dyeing pre-treatment carries out all in the basic conditions, as insufficient in the washing after concise and Alkali reduction, the pH value that so dyes in slightly acidic bath is difficult to control, and causes that dyeing colo r light between cylinder from cylinder is different, dyeing repeatability reduces.
And present stage DISPERSE DYES basic dyeing be also one of the high efficiency shortened process, energy-saving and emission-reduction dyeing and finishing technique that dyeing is discussed warmly.Domestic and international many scientific research personnel have carried out a series of research to alkali resistance disperse dye, in succession develop the dyestuff and technique that dye under some are applicable to alkali condition.But corresponding dye species is still little at present, chromatogram is incomplete, and the terylene basic dyeing promoted need adopt special dyeing auxiliary agent to coordinate dyeing, and the performance of dyeing assistant goes back less stable at present.And it is too responsive to pH value at present also to there is dyestuff, easily produce cylinder poor, unstable product quality, can not stablize upper dye in highly basic (as NaOH) system, the dye-uptake of dyestuff is lower than two-bath process, shortcoming that the control of fabric feeling, capillary effect is not good.
Summary of the invention
And UNIVADINE SD synthetic fiber refining-dyeing assistant is applicable to PES, PBT, the synthetic fiber of PTT and PA class and BLENDED FABRIC refining-disperse dyeing single bath process processing thereof have removal impurity (as oil or the knitting oil of spinning, wax etc.), emulsion dispersion leftover slurry and the precipitation preventing oligomer, the effect of crystallization or gathering and dyeing level dyeing, and this auxiliary agent is applicable to the dyeing and finishing processing under acid condition, namely advantage (the favorable reproducibility of DISPERSE DYES acid dyeing is embodied, dye-uptake is high, chromatogram is complete, bright-colored) embody again some advantages (1 of DISPERSE DYES basic dyeing, decrease refinery practice to be conducive to, energy-saving and cost-reducing, reduce discharge of wastewater, enhance productivity.2, a difficult problem for dyeing terylene oligomer is effectively overcome.3, the residual caused look flower of finish, polymer and the slurry that fabric causes because pre-treatment is bad, uneven dyeing, slurry flower is solved.)
The application of dyeing assistant UNIVADINE SD in high-count and high-density polyester fabric dyeing and finishing method, is included in the single bath process step adopting refining oil removing+dyeing+reduction cleaning, described single bath process process prescription and condition as follows:
described single bath process concrete operations are as follows: by DISPERSE DYES, UNIVADINE SD, and buffer RUCO-ACID ABS is in 40 DEG C of mixing, and be heated to 130 DEG C of insulation 50min with the programming rate of 1.5-2 DEG C/min, pH value maintains 4.5, and bath raio is 1:8; Then be cooled to 70-80 DEG C, add acidic reduction agent ERIOPON RC, insulation 20min, draining.
Described DISPERSE DYES proportioning is:
TERASIL ORANGE SD%(o.w.f) 2.8
TERASIL RUBINE SD%(o.w.f) 0.35
TERASIL BLUE SD%(o.w.f) 1.5。
Open width decrement Desizing Step is also comprised before described single bath process.
Technology preparation (g/L) and the condition of described open width decrement Desizing Step are as follows:
Described high-count and high-density polyester fabric is selected from fineness of yarn and is less than 50D, and Density is greater than the polyester fabric of the various plain weaves of 290T, twill or other alternative construction.
Accompanying drawing explanation
Accompanying drawing 1: the process curve of traditional high-count and high-density polyester fabric
Accompanying drawing 2: process curve of the present invention
Accompanying drawing 3: cloth cover slurry quantitative assay DIN 54285 of the present invention
Accompanying drawing 4: destarch design sketch, the first from left is grey cloth, and the second from left is destarch design sketch after common open-width desizing, and right two is destarch design sketch after common open width+refining, and right one is open width+UNIVADINE SD destarch design sketch of the present invention
Accompanying drawing 5: the dispersion and emulsion of greasy dirt can be tried hard to, the first from left is that common degreaser emulsifying power is tried hard to, and centre is tried hard to for adding 2g/L UNIVADINESD emulsifying power, and right one is non-adding assistant figure
Accompanying drawing 6: dispersibility suction filtration resolution chart, the left side is non-adding assistant design sketch, and the right is for adding the design sketch of 2g/L UNIVADINE SD
Accompanying drawing 7: dispersibility activated carbon method resolution chart, the left side is non-adding assistant design sketch, and the right is for adding the design sketch of 2g/L UNIVADINE SD
Accompanying drawing 8: to the removal effect figure of oligomer, the left side is non-adding assistant design sketch, and the right is for adding the design sketch of 2g/L UNIVADINE SD
Detailed description of the invention
1 test
1.1 materials, medicine and instrument
Material 310T plain weave delustring Polyester Taffeta 50D/72F (FDY) * 50D/72F (FDY), 620/10cm*50 root/10cm, grammes per square metre 67g/m 2, door width 168cm
Dye dispersion dyestuff TERASIL SD series (Hensel steps weaving dyeization)
Medicine UNIVADINE SD (Hensel step weaving dyeization), liquid caustic soda, tertiary sodium phosphate, the oxidation desizing agent TF-127(development of evil in febrile disease), ice vinegar, sodium hydrosulfite, acidic reduction agent ERIOPON RC (Hensel steps weaving dyeization), chelated dispersants INVATEXED (Hensel dyeization of weaving advanced in years), the degreaser TF-115C(development of evil in febrile disease), buffer RUCO-ACID ABS (Rudoiph's chemical industry), levelling agent RUCOGAL SBM (Rudoiph's chemical industry)
Instrument and equipment High Temperature High Pressure overflow dyeing machine (Taiwan Dong Wu Industries, Inc), setting machine (Taiwan power root), open-width desizing range (Taiwan letter is flourish), Startlet DL-1800 type infrared ray dyeing proof machine (large Lin Sidale company of Korea S), UltraScan XE colour photometer (HunterLab company of the U.S.)
1.2 method of testing
1) water-fastness COLOR FASTNESS is by ISO105/C06:2010 " textile color stability tests C06 part: resistance to family and commercial laundering COLOR FASTNESS .A2S "
2) colour fastness to perspiration is by ISO105/E04:2008 " textile color stability tests E04 part: colour fastness to perspiration "
3) crock fastness is according to GB/T3920-1997, measures the crock fastness before and after fixation with Y507L type crock fastness instrument.
4) colour index, adopts UltraScan XE colour photometer to measure, surperficial that color depth K/S value represents, color parameter △ L*, △ a*, △ b* and △ E value.
1.3 embodiments one: dyeing and finishing technology
1.3.1 traditional handicraft
1) open width decrement destarch
Technology preparation (g/L) and condition as follows:
2) refining oil removing
Technology preparation (g/L) and condition as follows
3) dye
Technology preparation and condition as follows
4) soap
Technology preparation (g/L) and condition as follows
1.3.2 novel process
1) open width decrement destarch
Technology preparation (g/L) and condition as follows:
2) refining oil removing+dyeing+reduction cleaning single bath process
Technology preparation and condition as follows
1.3.3 process curve contrast
1) (tradition) high-count and high-density polyester fabric: the open-width desizing+refining+technique that dyes+soap (see accompanying drawing 1)
2) (novel) high-count and high-density polyester fabric: open-width desizing+single bath process technique that dyes+soap (see accompanying drawing 2)
By accompanying drawing 1, the process curve of 2 is known, and traditional process route needs to carry out refining successively after open-width desizing, dyeing, reduction cleaning, warm water washing, cold water flush, neutralization procedure, complex procedures, and full operation required time is about 240-260 minute; And process route of the present invention adopts single bath process to complete disposable for above-mentioned steps, simple to operation, full operation required time is only
150-170 minute.
2, embodiment 2
2.1, the optimization of technique
Take yarn as the fabric of warp, before weaving, all have to pass through starching process, to improve the brute force of warp thread, ABRASION RESISTANCE and smooth degree, thus reduce warp end break, ensureing weaves cotton cloth carries out smoothly.And fiber is in spinning or be starching and the finish weaved high speed and add or emulsified wax.On the one hand during open width decrement destarch pre-treatment, auxiliary agent groove is generally periodic replacement in 7-8 days, and there is the chemical sizwe excessive concentration that auxiliary agent groove dissolves, these chemical sizwes are all high molecular polymers, and viscosity is high, easily condense, and easily causes the counter of slurry to be stained with cloth face phenomenon.On the other hand spinning oil is when open-width desizing process, interpolation except oil assistant the greasy dirt on fabric well can not be soaked, permeate, emulsification, dispersion, solubilising, the effect such as washing, finish and greasy dirt are removed from fiber and fabric.
One, the destarch effect of UNIVADINE SD
1. cloth cover slurry quantitative assay
Buffer RUCO-ACID ABS (g/L) 1.5
UNIVADINE SD(g/L) 2
PH value 4-5130 DEG C is run 50 minutes
300T polyester filament woven fabric slurry content situation (cloth cover slurry quantitative assay DIN54285) is see accompanying drawing 3.
2. cation dyes colouring (concrete grammar is as follows: adopt cation dyes 2GL red, 0.02%(o.w.f), bath raio 1:50, pH value 4.5, process conditions 50 DEG C, 10min, washing, viewing cloth cover shade after drying, cloth cover is redder shows that cloth cover residual slurry is more, otherwise fewer.) see Fig. 4, can find out, after open-width desizing, cloth cover also has certain residual slurry, can affect the quality of textile dyeing.And after refining with add UNIVADINE SD and dye identical with the destarch effect of bathing.Prove that this auxiliary agent has excellent emulsification and dispersed paste ability, can not refining direct dyeing be carried out, decrease process time and energy resource consumption.
Two, the oil removing performance of UNIVADINE SD
100 DEG C are run 40 minutes as Fig. 5: deoil and dispersion and emulsion ability to greasy dirt
Can find out in 5 from the graph, have fabulous emulsion dispersion effect to the greasy dirt in water after adding UNIVADINE SD, solution surface is not floated phenomenon.Prove that this auxiliary agent can effective oil removing and reduce the precipitation of oil, have good emulsification, dispersibility, can effectively overcome because pre-treatment effect of deoiling is bad, look irregular problem is inhaled in caused greasy dirt spot and level dyeing.
The dyeability of 2.2 UNIVADINE SD
One, dispersibility
1) suction filtration test
1.5g/L DISPERSE DYES TERASIL BLUE SD
Bath raio 1:10
PH value 4-5
130 DEG C run 30 minutes, get 20 milliliters filter after, filter paper is dried.As Fig. 6:
2) absorbent charcoal method
As Fig. 7: RBN 101/AE-1996 (36 hours)
The result of Fig. 6 and Fig. 7 illustrates: this auxiliary agent has outstanding dispersibility, the risk that can reduce dye aggregation He attach, and makes dye bath keep stable and is beneficial to level dyeing, stop the impurity removed to precipitate again.
Two, to the removal effect of oligomer: as Fig. 8: the microphoto of polyster fibre oligomer
Data as can be seen from Fig. 6, Fig. 7, Fig. 8, after adding UNIVADINE SD, the content of fabric face oligomer reduces greatly, can effectively disperse and the suspension of stable oligomer, prevent the precipitation of oligomer, crystallization or gathering, overcome the grey flour presented at fabric face.And in normal dyeing process, oligomer can constantly be separated out, diffuse in dye bath or be deposited on fabric face, causing the outward appearance defect of the rear fabric of dyeing.
Three, slow metachromia
TERASIL BLUE SD 1%( o.w.f)
SD 2g/L
Buffer RUCO-ACID ABS (g/L) 1.5
Bath raio 1:10, heat up 2 DEG C/min, in each stage sampling colour examining (as table 1)
Cloth cover Apparent Depth K/S value UNIVADINE SD Blank
90℃ X 10 min 0.081 0.102
100℃ X 10 min 0.65 0.95
110℃ X 10 min 1.78 2.16
120℃ X 10 min 2.54 2.89
130℃ X 10 min 3.01 3.13
Illustrated by table 1 data, mainly dyestuff is at the absorption uniformity coefficient of fiber surface to determine upper dye level-dyeing property in dyeing, and it can be seen from the table, during 90-110 DEG C, in blank bath, on dyestuff, dye is obviously accelerated, because be at this moment the cause that dyestuff starts to fibrous inside diffusion.And add UNIVADINE SD synthetic fiber refining-dyeing assistant, effectively suppress the association rate of dyestuff and fiber, and alternately stained with fiber along with the temperature rising levelling agent of dye liquor and dyestuff, illustrate that this auxiliary agent has reasonable slow metachromia,
Effectively can control the dye-uptake of dyestuff, guarantee the uniformity of adsorbing.
2.3, energy contrast
Table 2: new technology and the consumption of traditional terylene process water contrast as follows:
Table 3: new technology and the energy resource consumption of traditional terylene technique contrast as follows:
Table 4: traditional handicraft and new technology is energy-conservation, comparison sheet of economizing on water:
Remarks: the textile industry standard FZ/T01002-2010 that (1) above data are announced with reference to the Ministry of Industry and Information Technology of the People's Republic of China (PRC).
(2) above-mentioned fabrics is 100-140g/m 2, door width is less than 1.6 meters, every hundred meters of calculating.
(3) steam used in above-mentioned technique, electricity, water are all rolled over for standard coal calculates.
As can be seen from table 2, table 3, table 4 data, Novel disperse dyestuff refining one-pass bath method for dyeing technique be low steam consumption quantity, a sewage discharge less energy-conserving and environment-protective, green clearer production technology.
2.4, COLOR FASTNESS contrast
The COLOR FASTNESS effect of contrast traditional handicraft and novel process:
Washing result is as following table 5:(ISO/C06A2S)
PERSPIRATION COLOR FASTNESS result is as following table 6:ISO105/C06:2010
Colorfastness to rubbing result is as following table 7:ISO105X12:2002
As can be seen from data in showing above, novel process is than traditional handicraft, unchanged on Washing, perspiration fastness, crock fastness, can energy efficient very well, emissions reduction.
2.5, the application of UNIVADINE SD is on the impact of fabric dye-uptake
The change in concentration of the use of levelling agent in dyeing course can produce certain impact, in table 8 to dye-uptake K/S value.From table 8, along with the lifting of refining-dyeing leveling agent UNIVADINE SD mass concentration, fabric face obtains color depth (K/S) value to be reduced gradually, raising along with auxiliary dosage is described, the effect of slow dye is more and more obvious, be conducive to dyestuff and evenly go up dyeing and weaving thing, decrease that look colored, page is poor, color dot phenomenon.
The upper dye situation (situation of change of K/S value) of table 8 levelling agent consumption change
The coloured light result situation that table 9 DYED FABRICS is final
Note: carry out test and comparison as standard sample using the color sample of blank sample (non-adding assistant).
Learn from table 9, the dyeing colo r light of sample and intensity relatively, illustrate with now used additives and UNIVADINE SD have no significant change to the coloured light of DYED FABRICS and intensity.
3. conclusion
The new technologies such as current, international and domestic to ecological environment growing interest, energy-conservation, consumption reduction, environmental protection, short route are the inexorable trends of dyeing development.And traditional handicraft not only production efficiency is low, process route is tediously long, also need to consume a large amount of water, electricity, coal, steam and workman labour, and a large amount of sewage can be produced after washing, larger waste water control cost [11] need be spent, and the enforcement of novel process can improve the productivity ratio of 30%, reduce the water consumption of 50% and the energy consumption of 25%, there is very large energy-saving and emission-reduction advantage, meet the development trend of present dyeing, have broad application prospects and promotion potential.

Claims (5)

1. the application of dyeing assistant UNIVADINE SD in high-count and high-density polyester fabric dyeing and finishing method, it is characterized in that the manufacture method of described high-count and high-density polyester fabric comprises the single bath process step adopting refining oil removing+dyeing+reduction cleaning, described single bath process process prescription and condition as follows:
Described single bath process concrete operations are as follows: by DISPERSE DYES, UNIVADINE SD, and buffer RUCO-ACID ABS is in 40 DEG C of mixing, and be heated to 130 DEG C of insulation 50min with the programming rate of 1.5-2 DEG C/min, pH value maintains 4.5, and bath raio is 1:8; Then be cooled to 70-80 DEG C, add acidic reduction agent ERIOPON RC, insulation 20min, draining.
2. the application of dyeing assistant UNIVADINE SD in high-count and high-density polyester fabric dyeing and finishing method as claimed in claim 1, is characterized in that described DISPERSE DYES proportioning is:
3. the application of dyeing assistant UNIVADINE SD in high-count and high-density polyester fabric dyeing and finishing method as claimed in claim 2, also comprises open width decrement Desizing Step before it is characterized in that described single bath process.
4. the application of dyeing assistant UNIVADINE SD in high-count and high-density polyester fabric dyeing and finishing method as claimed in claim 3, it is characterized in that the technology preparation of open width decrement Desizing Step and condition as follows:
5. the application of dyeing assistant UNIVADINE SD in high-count and high-density polyester fabric dyeing and finishing method as claimed in claim 4, it is characterized in that described high-count and high-density polyester fabric is selected from fineness of yarn and is less than 50D, Density is greater than the polyester fabric of the various plain weaves of 290T, twill or other alternative construction.
CN201310079315.5A 2013-03-13 2013-03-13 Application of dyeing auxiliary agent Univadine SD in high count high density polyester lining dyeing and finishing Active CN103215824B (en)

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CN103590271B (en) * 2013-10-16 2016-03-09 河南工程学院 Alkali Weight Reduction Treatment of Polyester and dyeing one bath one step low temperature process method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101397714A (en) * 2007-09-30 2009-04-01 上海嘉乐股份有限公司 Method for producing coarse gauge double yarn galling flannel
CN101503853A (en) * 2008-02-04 2009-08-12 上海德桑印染有限公司 Method for processing fabric by scouring dyeing one bath
CN101845761A (en) * 2010-05-26 2010-09-29 何鹰 Acidic reduction cleaner

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101397714A (en) * 2007-09-30 2009-04-01 上海嘉乐股份有限公司 Method for producing coarse gauge double yarn galling flannel
CN101503853A (en) * 2008-02-04 2009-08-12 上海德桑印染有限公司 Method for processing fabric by scouring dyeing one bath
CN101845761A (en) * 2010-05-26 2010-09-29 何鹰 Acidic reduction cleaner

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