CN101200859A - Salt-free pad steam continuous dyeing method for active dye - Google Patents
Salt-free pad steam continuous dyeing method for active dye Download PDFInfo
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- CN101200859A CN101200859A CNA2006101681212A CN200610168121A CN101200859A CN 101200859 A CN101200859 A CN 101200859A CN A2006101681212 A CNA2006101681212 A CN A2006101681212A CN 200610168121 A CN200610168121 A CN 200610168121A CN 101200859 A CN101200859 A CN 101200859A
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- reactive dyes
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Abstract
The present invention relates to a continuous saltless pad-steam dyeing method with reactive dyes, which belongs to the novel technical field of textile printing and dyeing. After being singed, desized, boiled, bleached and mercerized, the half-finished product of cellulosic fibre woven fabric is dyed in the process of the continuous dyeing technique of padding, steam fixation, water washing, soaping, water washing and drying by the reactive dyes. The half-finished product of the preprocessed cellulosic fibre woven fabric is produced by pad dyeing, steaming and water washing, wherein, dyeing solution is composed of M reactive dyes, leveling agent, fixation alkali agent and water, and the mixture ratio is as follows: M reactive dyes: 0.01 percent to 10 percent, leveling agent: 0.1 percent to 0.2 percent, fixation alkali agent: 1.5 percent to 4 percent, and water: balance. The method is different from the conventional continuous dyeing technique of padding, drying, padding and steaming, which uses reactive dyes, and also different from the shortened wet-steaming technique with reactive dyes. On the conventional continuous padding machine, the novel method can fulfill the whole process of reactive dyeing without a hot-air padding machine and only with a developing and soaping range, thus greatly saving energy and reducing cost.
Description
Technical field
The invention belongs to technical field of textile printing, particularly a kind of salt-free pad steam continuous dyeing method for active dye.
Technical background
The existing conventional REACTIVE DYES roll baking roll steam technology be five step process promptly: roll, dry by the fire, roll, steam, wash.This process route is long, the cost height; Technology controlling and process point is many, the probability height of quality problems occurs.
1, printing and dyeing industry is faced with following situation in recent years:
The dyeing color and luster is many, and processing variety is and continues to increase;
Require textiles to reach higher fastness ability;
Product requirement is delivered goods soon;
Environmental regulation is more and more stricter;
The manufacturing batch work significantly reduces;
Production capacity is crossed victory;
The America and Europe limits;
Appreciation of the RMB, export rebate rate reduces;
A cost such as the energy, dyestuff, labour cost rises, and profit descends;
One of main pressure that dyeing faced is reduction in batches.Because equipment investment requires that certain production capacity is arranged, therefore, the printing and dyeing processing output directly influences usage ratio of equipment.
2, the wet short technology of steaming is promoted difficulty
On the nineteen ninety-five ITMA (TIMA) held of Milan, ITA, the Econtrol technology that German Monforts (Monforts) company and Zeneca company (being the part of present De Sida company) have showed the REACTIVE DYES continuous knot dyeing of two companies cooperative development.And in before several years, REACTIVE DYES continuous knot dyeing technology technical progress is very little, does not almost have big innovation, and realizes industrialized application.
Econtrol technology provides the advantage of Controlled Coloration (controlled dyeing) to the dyer author, and the innovative means of being designed and developed by Monforts.So far, 65 are only sold and installed in the whole world, and in China till now for having only 4 to what only buy and install, only two of domestic imitation, its reason: (1), import equipment cost height (nearly 8,000,000 RMB) (2), technique controlling difficulty are big.(3), the home equipment improvement that is left to be desired.
In view of the foregoing, it is necessary to invent a kind of REACTIVE DYES continuous dyeing method of more economical shorter flow process.The present invention rolls and steams five step process and change the step process method of rolling, steam, give a baby a bath on the third day after its birth into by using methods such as new dyestuff, fixation alkaline agent, auxiliary agent will roll baking, has shortened process route, has improved quality, has reduced cost.
Summary of the invention
The technology of the present invention problem provides fixation alkaline agent, dyestuff and the control process parameters thereof of using preparation and improves existing five step production technologies, shortens to three step production technologies.Mainly be to have changed five traditional step production technologies, its dyestuff, auxiliary agent and waste water, toxic emission are reduced greatly, improved the pollution of environment, adapted to environmental protection requirement, shorten simultaneously the flow process time of production technology greatly, reduced cost, had social benefit and economic benefit.Can adapt to the market development requirement of the many kinds of small lot.
In order to achieve the above object, realize by the following technical solutions: a kind of salt-free pad steam continuous dyeing method for active dye, comprise cellulose base fiber fabric semi-products with pre-treatment, make through padding dye liquor, vapour steaming colour fixing and three steps of washing, wherein dye liquor is made up of REACTIVE DYES, levelling agent, fixation alkaline agent and water, and its proportioning is as follows:
REACTIVE DYES 0.01-10%
Levelling agent 0.1-0.2%
Fixation alkaline agent 1.5-4%
Water surplus
Dyestuff is a M type REACTIVE DYES, i.e. a chloro-s-triazine and beta-hydroxy second sulfone sulfate double-active radical, and main REACTIVE DYES producer all produces both at home and abroad.
Fixation alkaline agent is the CJ-R that Yongji Wan Xiang company produces, and main component is the mixture of carboxylic acid sodium and caustic soda.
Levelling agent is a fat alcohol polyethylene ether for paregal O, the Main Ingredients and Appearance that the auxiliary reagent factory, Shanghai produces, and molecular formula is: C
nH
2n+1(OCH
2CH
2)
mOH.
The temperature of padding is a room temperature, and steam temperature is 100-102 ℃, and steaming time is 90 seconds.
Because dye fixing was finished in 90 seconds, therefore, had selected M type REACTIVE DYES for use.
Common rolling dried by the fire the auxiliary agent that rolls the use of steaming dyeing, all can use in the salt-free pad steam dyeing.
The fixation alkaline agent consumption changes according to dye dosage and increases and decreases, and amount ranges is at 1.5-4%.
Concrete salt-free pad steam technological process is: pad dye liquor, decatize (100 ℃-102 ℃ 90 seconds), wash, soap, heat is washed, cold wash, oven dry.
Conventional REACTIVE DYES roll baking roll steam technology be five step process promptly: roll, dry by the fire, roll, steam, wash, the salt-free pad steam work simplification be three step process promptly: roll, steam, wash.Salt-free pad steam technology is on the continuous pad-dyeing range of routine, has only just finished the overall process of REACTIVE DYES continuous dyeing with developing and soaping range without padding machine.
The applicant is according to the dyeing theory of REACTIVE DYES, and development test salt-free pad steam technology is carried out the screening of dyestuff and auxiliary agent through test dye, additive performance repeatedly, and success of the test salt-free pad steam continuous dyeing technology has realized industrialized mass production.
Beneficial effect of the present invention: economy; Color and luster variety renovation efficiently; Use easy; Be applicable to fresh colour, very shallow and very dark color and luster; Excellent reappearance is to obtain high production reliability; Environmentally friendly; Technology to fastness ability without limits; Process time is short.
Salt-free pad steam technology dyeing finished product after testing, to roll every fastness index of steaming technology dyeing finished product in full accord with rolling baking.Is 4 grades with the evaluation variable color with gray scale evaluation head and the tail aberration, color light stabilizing.Salt-free pad steam technology is all carried out under hygrometric state condition to the fixation process of dyestuff from the mixed liquor that pads dyestuff and fixation alkaline agent, does not exist to roll to dry by the fire to roll the migration problem of technology dyestuff in the padding machine drying course of steaming, and the fabric imbue is good simultaneously.
Adopt salt-free pad steam technology, can the woven fabric of all fibres cellulose fiber be dyeed, yarn with different, different grammes per square metres all can.Fabric weight is at 70-500g/m
2
Salt-free pad steam continuous pad-dyeing range rolls baking and rolls and steam continuous pad-dyeing range and compare with one, and this technology has been saved hot flue padding machine, only with the reduction soaper, under normal operation, every equipment year is saved 3847.5 tons of steam, economizes on water 10125 tons, 19.44 ten thousand degree that economize on electricity, 360 tons of joint salt.
Salt-free pad steam technology dyeing, environmental friendliness, energy-conservation, consumption reduction, effect are remarkable.The industrialized producing technology environmental characteristics has become more and more important factor.When selecting to optimize dyeing, need to consider the environmental protection characteristic of this technology, wherein main standards is the pollution condition of energy consumption, chemicals usage, draining and exhaust.What will consider in addition is whether environment amenable technology has economy.Satisfy above-mentioned requirements fully and roll steaming technology.
With roll baking roll steam technology different be that salt-free pad steam technology need not to use salt.Roll and steam in the technology, rolling baking if fabric weight is 350g/m
2, the pad dyeing rate is 70%, and the salt consumption is 250g/L, and the required salt amount of 1,000,000 square meter fabrics that then dyes adds up to 61000kg.
Salt-free pad steam technology and routine are rolled baking and are rolled and steam technology and compare joint and removed a hot flue padding machine, have saved cost.Salt-free pad steam technology is compared only use reduction soaper, the infrared ray heating of the wet short steaming of saving and humidity, temperature control part branch with the short technology of steaming that wets.
Specific embodiments
Embodiment 1: a kind of salt-free pad steam continuous dyeing method for active dye, use following colouring method, through padding dye liquor, decatize, wash, soap, wash, drying and form.Wherein the dye liquor proportioning is as follows:
M type REACTIVE DYES 5%
Paregal O 0.1%
Fixation alkaline agent 2%
Water 92.9%
Dyestuff is a M type REACTIVE DYES, i.e. a chloro-s-triazine and beta-hydroxy second sulfone sulfate double-active radical.Fixation alkaline agent is the CJ-R that Yongji Wan Xiang company produces, and main component is the mixture of carboxylic acid sodium and caustic soda.Levelling agent is a fat alcohol polyethylene ether for paregal O, the Main Ingredients and Appearance that the auxiliary reagent factory, Shanghai produces, and molecular formula is: C
nH
2n+1(OCH
2CH
2)
mOH.
The temperature of padding: room temperature, the temperature of decatize: 100 ℃-102 ℃, the time: 90 seconds.
Embodiment 2: a kind of salt-free pad steam continuous dyeing method for active dye, use following colouring method, through padding dye liquor, decatize, wash, soap, wash, drying and form.Wherein the dye liquor proportioning is as follows:
M type REACTIVE DYES 8%
Paregal O 0.15%
Fixation alkaline agent 3%
Water 88.85%
Dyestuff is a M type REACTIVE DYES, i.e. a chloro-s-triazine and beta-hydroxy second sulfone sulfate double-active radical.Fixation alkaline agent is the CJ-R that Yongji Wan Xiang company produces, and main component is the mixture of carboxylic acid sodium and caustic soda.Levelling agent is a fat alcohol polyethylene ether for paregal O, the Main Ingredients and Appearance that the auxiliary reagent factory, Shanghai produces, and molecular formula is: C
nH
2n+1(OCH
2CH
2)
mOH.
The temperature of padding: room temperature, the temperature of decatize: 100 ℃-102 ℃, the time: 90 seconds.
Claims (2)
1. a salt-free pad steam continuous dyeing method for active dye comprises the cellulose base fiber fabric with pre-treatment, and through padding dye liquor, decatize and giving a baby a bath on the third day after its birth to go on foot and make, wherein dye liquor is made up of REACTIVE DYES, levelling agent, fixation alkaline agent and water, and its proportioning is as follows:
M type REACTIVE DYES 0.01-10%
Levelling agent 0.1-0.2%
Fixation alkaline agent 1.5-4%
Water surplus
Pad temperature: room temperature, steam temperature: 100-102 ℃, steaming time: 90 seconds.
2. according to the salt-free pad steam continuous dyeing method for active dye of claim 1, wherein said dyestuff is a M type REACTIVE DYES, i.e. a chloro-s-triazine and beta-hydroxy second sulfone sulfate double-active radical; Fixation alkaline agent is the CJ-R that Yongji Wan Xiang company produces, and main component is carboxylic acid sodium and caustic soda; The paregal O that levelling agent is produced for the auxiliary reagent factory, Shanghai, Main Ingredients and Appearance is a fat alcohol polyethylene ether, molecular formula is:
C
nH
2n+1(OCH
2CH
2)
mOH。
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CN2006101681212A CN101200859B (en) | 2006-12-15 | 2006-12-15 | Salt-free pad steam continuous dyeing method for active dye |
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CN101200859A true CN101200859A (en) | 2008-06-18 |
CN101200859B CN101200859B (en) | 2011-04-20 |
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Cited By (19)
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CN101922121A (en) * | 2010-08-11 | 2010-12-22 | 浙江理工大学 | New dyeing method of active dye taking methylsiloxane as medium |
CN102191642A (en) * | 2010-03-01 | 2011-09-21 | 温国俊 | Reactive dye pad dyeing and steaming process |
CN102199886A (en) * | 2011-05-23 | 2011-09-28 | 东华大学 | Reactive dye salt-free pad dyeing method |
CN102268204A (en) * | 2011-05-31 | 2011-12-07 | 沈阳市中发金属结构件厂 | Anti-theft label ink |
CN102504597A (en) * | 2011-12-02 | 2012-06-20 | 西南大学 | Preparation method of hydrophobic controllable reactive dye D-W-R |
CN102758326A (en) * | 2011-04-28 | 2012-10-31 | 孚日集团股份有限公司 | Reactive dye continuous pad-dyeing shorted and wet steaming machining process for towel and quilt fabrics |
CN102912654A (en) * | 2012-11-09 | 2013-02-06 | 愉悦家纺有限公司 | Dyeing method for fabric |
CN102926235A (en) * | 2012-11-08 | 2013-02-13 | 绍兴文理学院 | Liquid mixed base for activated dye high temperature dyeing and preparation method and application thereof |
CN104060487A (en) * | 2014-06-25 | 2014-09-24 | 太仓市虹鹰印花有限公司 | Random printing technology |
CN104532499A (en) * | 2015-01-23 | 2015-04-22 | 天津工业大学 | Padding, wet steaming and dyeing method of reactive dye |
CN105507028A (en) * | 2016-01-14 | 2016-04-20 | 天津工业大学 | Reactive dyeing method for cellulose fiber fabric |
CN108560289A (en) * | 2018-05-03 | 2018-09-21 | 鲁丰织染有限公司 | Pure cotton activity salt-free dyeing liquid, pure-cotton fabric and technique using its dyeing |
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CN110644167A (en) * | 2019-09-12 | 2020-01-03 | 青岛大学 | Salt-free continuous pad dyeing process for cellulose fiber knitted fabric |
CN111676624A (en) * | 2020-06-04 | 2020-09-18 | 如皋市协和印染有限公司 | Long-vehicle pad dyeing wet-to-wet process |
CN113529440A (en) * | 2020-04-16 | 2021-10-22 | 华纺股份有限公司 | Wet fixation dyeing method of reactive dye |
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Family Cites Families (3)
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US5603736A (en) * | 1992-04-27 | 1997-02-18 | Burlington Chemical Co., Inc. | Liquid alkali for reactive dyeing of textiles |
CN1308542C (en) * | 2005-04-15 | 2007-04-04 | 夏建明 | Liquid fixation alkaline agent for activated dyes of coloration |
CN100427672C (en) * | 2006-03-10 | 2008-10-22 | 苏明辉 | Liquid dyeing base (SN) for active dye dying |
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2006
- 2006-12-15 CN CN2006101681212A patent/CN101200859B/en not_active Expired - Fee Related
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CN102191642A (en) * | 2010-03-01 | 2011-09-21 | 温国俊 | Reactive dye pad dyeing and steaming process |
CN101922121B (en) * | 2010-08-11 | 2012-09-26 | 浙江理工大学 | New dyeing method of active dye taking methylsiloxane as medium |
CN101922121A (en) * | 2010-08-11 | 2010-12-22 | 浙江理工大学 | New dyeing method of active dye taking methylsiloxane as medium |
CN102758326A (en) * | 2011-04-28 | 2012-10-31 | 孚日集团股份有限公司 | Reactive dye continuous pad-dyeing shorted and wet steaming machining process for towel and quilt fabrics |
CN102199886A (en) * | 2011-05-23 | 2011-09-28 | 东华大学 | Reactive dye salt-free pad dyeing method |
CN102199886B (en) * | 2011-05-23 | 2012-08-29 | 东华大学 | Reactive dye salt-free pad dyeing method |
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CN102504597B (en) * | 2011-12-02 | 2013-11-27 | 西南大学 | Preparation method of hydrophobic controllable reactive dye D-W-R |
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CN110644167A (en) * | 2019-09-12 | 2020-01-03 | 青岛大学 | Salt-free continuous pad dyeing process for cellulose fiber knitted fabric |
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