CN109267393A - A kind of preparation method of the oil removing level dyeing compound emulsifying agent for dacron - Google Patents

A kind of preparation method of the oil removing level dyeing compound emulsifying agent for dacron Download PDF

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Publication number
CN109267393A
CN109267393A CN201810836634.9A CN201810836634A CN109267393A CN 109267393 A CN109267393 A CN 109267393A CN 201810836634 A CN201810836634 A CN 201810836634A CN 109267393 A CN109267393 A CN 109267393A
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Prior art keywords
vinyl phenol
triphenyl vinyl
oxygen propylene
oil removing
phenol polyoxyethylene
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CN109267393B (en
Inventor
刘作平
孙思恒
邓斐
刘晓芸
吕晓辉
姚庆才
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ZHEJIANG SILK TECHNOLOGY Co.,Ltd.
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ZHEJIANG SILK INSTITUTE LIGHT TEXTILE MATERIAL Co Ltd
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/44General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/60General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders using compositions containing polyethers
    • D06P1/613Polyethers without nitrogen
    • D06P1/6131Addition products of hydroxyl groups-containing compounds with oxiranes
    • D06P1/6135Addition products of hydroxyl groups-containing compounds with oxiranes from aromatic alcohols or from phenols, naphthols
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/44General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders
    • D06P1/60General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed using insoluble pigments or auxiliary substances, e.g. binders using compositions containing polyethers
    • D06P1/613Polyethers without nitrogen
    • D06P1/6131Addition products of hydroxyl groups-containing compounds with oxiranes
    • D06P1/6133Addition products of hydroxyl groups-containing compounds with oxiranes from araliphatic or aliphatic alcohols
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06PDYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P3/00Special processes of dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form, classified according to the material treated
    • D06P3/34Material containing ester groups
    • D06P3/52Polyesters

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Coloring (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Abstract

The present invention relates to a kind of preparation methods of oil removing level dyeing compound emulsifying agent for dacron, belong to textile auxiliary field.Oil removing and dyeing are carried out in two steps in traditional handicraft, and production procedure is long, and the water power of consumption is more.Compound emulsifying agent is mixed by following mass percentage in the present invention: triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether 18~22%, triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate 8~12%, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate 8~12%, isomerous tridecanol polyoxyethylene ether 3~7%, surplus are water.The compound emulsifying agent is not phosphorous, with good except oiliness, slow metachromia and migration property, and influences on the dye-uptake of dyestuff small.Meanwhile oil removing and dyeing are combined into one by the present invention, are shortened dyeing and finishing technology process, are improved production efficiency, reduce production cost, have achieved the purpose that energy-saving and emission-reduction.

Description

A kind of preparation method of the oil removing level dyeing compound emulsifying agent for dacron
Technical field
The present invention relates to textile auxiliary fields, and in particular to a kind of oil removing level dyeing compound emulsifying agent for dacron Preparation method.
Background technique
All contain phosphorus for the degreaser and levelling agent of the better performances in textile processing use currently on the market, these Phosphorus, which is discharged into water body, easily causes water eutrophication, causes aquatic ecosystem species distribution unbalance, destroys Aquatic Ecosystem 2 The flowing of the substance and energy of system, therefore the textile auxiliary that textile processing uses be of great significance without phosphatization.
Terylene is an important species in synthetic fibers, and dyeing generally uses disperse dyes.But in the dyeing of terylene Cheng Zhong, often will appear specking and item spends equal dyeing defects.There are many reason of causing uneven dyeing, including pre-treatment oil removing is not Only, foam is too high in dye liquor, and dispersion stabilization difference can all cause uneven dyeing to disperse dyes at high temperature.In order to avoid dyeing not The generation of even phenomenon, traditional solution have: pre-treatment is using degreaser the oil on fabric except clean;Addition defoaming agent subtracts Foam in few dye liquor;Addition levelling agent delays the dyeing rate of dyestuff.Therefore it is all good to remove oiliness level-dyeing property for exploitation, and foam is low Product it is necessary.
Oil removing and dyeing are carried out in two steps in traditional handicraft, and production procedure is long, and the water power of consumption is more, such as application No. is 201710795797.2 Chinese patent.With the progress of production technology, the enhancing of people's environmental consciousness, national environmental protection regulation Improved day by day, the aggravation of market competition, the shortening process production technique that save the cost improves production efficiency increasingly receives an acclaim. In order to meet the needs of dye-works's oil removing one-pass bath method for dyeing technique, urgent need is developed a kind of without phosphorus, and foam is low, except oiliness and level-dyeing property are all Good compound emulsifying agent.
Summary of the invention
It is an object of the invention to overcome the above deficiencies in the existing technologies, and provide a kind of for dacron The preparation method of oil removing level dyeing compound emulsifying agent.
Technical solution used by the present invention solves the above problems is: a kind of oil removing level dyeing Composite Milk for dacron The preparation method of agent, which is characterized in that the preparation method includes the following steps:
(1) preparation of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether:
120 parts of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aethers and 13~15 parts of benzoic acid are added to reactor In;Stirring is started, 80 DEG C is warming up under nitrogen protection, is completely dissolved benzoic acid;Then 0.7~1 is added in the reactor Part p-methyl benzenesulfonic acid, is warming up to 100~115 DEG C, keeps the temperature 3~4 hours, reaction terminates, and obtains triphenyl vinyl phenol polyoxy second Alkene polyoxypropylene ester benzoic ether;
(2) preparation of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate:
By 120 parts of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aethers, 11~13 parts of sulfamic acids and 5~7 parts of urea It is added in reactor;Stirring is started, is warming up to 105~115 DEG C under nitrogen protection, keeps the temperature 3~4 hours, reaction terminates, and obtains three Styrylphenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate;
(3) triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether made from step (1), step (2) are made Triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate, the isomerous tridecanol polyoxyethylene polyethenoxy ether sulfuric acid obtained Sodium, isomerous tridecanol polyoxyethylene ether 1309 and water mix in proportion, and heating stirring is used to wash to uniformly mixed to get to one kind The oil removing level dyeing compound emulsifying agent of synthetic fibre fabric;Wherein each component mass percentage are as follows: triphenyl vinyl phenol polyoxyethylene is poly- Oxypropylene ester benzoic ether: 8~22%, triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate: 8~12%, isomery Tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate: 8~12%, isomerous tridecanol polyoxyethylene ether 1309:3~7%, surplus is Water.
The number of raw material is all mass fraction in above-mentioned steps (1) and step (2).
Furthermore, the general formula of molecular structure of the triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether Are as follows:
Wherein, m and n is integer;8≤m≤12,2≤n≤5.
Furthermore, the general formula of molecular structure of the triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate Are as follows:
Wherein, m and n is integer;8≤m≤12,2≤n≤5.
Furthermore, in the molecular structure of the isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate, ethylene oxide The number of base is 7~9, and the number of oxypropylene group is 1~3.
Compared with prior art, the present invention having the following advantages that and effect:
1, raw material triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether synthesized in the present invention, with tradition Levelling agent ingredient agriculture breast 600# compare, polyethenoxy ether and benzoate structure, polyethenoxy ether are introduced in molecular structure Structure effectively reduces oil removing level dyeing compound emulsifying agent spumescence, while benzoate structure has certain plasticising to dacron Effect improves the migration property of dyestuff while improving disperse dyes dispersibility.
2, raw material triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate synthesized in the present invention, and it is traditional Levelling agent composition B material is compared, and polyoxypropylene ether structure is introduced in molecular structure, improves dyestuff dispersibility and level-dyeing property.
3, the raw material tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate alkali resistance that the present invention uses is strong, good penetrability, no It is phosphorous, it is compared with conventional use of polyoxyethylene ether phosphate, meets environmental regulation requirement, advantageously reduce in dye house effluents Phosphorus content mitigates its wastewater treatment burden.
4, synthesis technology of the present invention is simply controllable, is suitble to industrialized production;Oil removing and dyeing are combined into one, shortened Dyeing and finishing technology process, improves production efficiency, reduces production cost, achieved the purpose that energy-saving and emission-reduction.
Specific embodiment
Below by embodiment, the present invention is described in further detail, following embodiment be explanation of the invention and The invention is not limited to following embodiments.
Embodiment 1.
1) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether and 130kg benzoic acid are added to reactor In;Stirring is started, 80 DEG C is warming up under nitrogen protection, is completely dissolved benzoic acid;Then 7kg is added in the reactor to first Benzene sulfonic acid is warming up to 100 DEG C, keeps the temperature 3 hours, reaction terminates, and obtains triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzene first Acid esters;
2) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether, 110kg sulfamic acid and 50kg urea are added Enter in reactor;Stirring is started, is warming up to 105 DEG C under nitrogen protection, keeps the temperature 3 hours, reaction terminates, and obtains triphenylethylene base benzene Phenol polyethenoxy polyoxypropylene ether ammonium sulfate;
It 3) will be three made from triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether made from step 1, step 2 Styrylphenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate, isomery Tridecanol polyoxyethylene ether 1309 and water mix in proportion: triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether 18%, triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate 8%, isomerous tridecanol polyoxyethylene polyethenoxy ether sulphur Sour sodium 8%, isomerous tridecanol polyoxyethylene ether 3%, surplus are water.Heating stirring is used for terylene to uniformly mixed to get one kind The oil removing level dyeing compound emulsifying agent of fabric.
Embodiment 2.
1) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether and 140kg benzoic acid are added to reactor In;Stirring is started, 80 DEG C is warming up under nitrogen protection, is completely dissolved benzoic acid;Then 8kg is added in the reactor to first Benzene sulfonic acid is warming up to 110 DEG C, keeps the temperature 3.5 hours, reaction terminates, and obtains triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzene Formic acid esters;
2) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether, 120kg sulfamic acid and 60kg urea are added Enter in reactor;Stirring is started, is warming up to 110 DEG C under nitrogen protection, keeps the temperature 3.5 hours, reaction terminates, and obtains triphenylethylene base Phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate;
It 3) will be three made from triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether made from step 1, step 2 Styrylphenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate, isomery Tridecanol polyoxyethylene ether 1309 and water mix in proportion: triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether 20%, triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate 10%, isomerous tridecanol polyoxyethylene polyethenoxy ether Sodium sulphate 9%, isomerous tridecanol polyoxyethylene ether 5%, surplus are water.Heating stirring is used to wash to uniformly mixed to get one kind The oil removing level dyeing compound emulsifying agent of synthetic fibre fabric.
Embodiment 3.
1) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether and 150kg benzoic acid are added to reactor In;Stirring is started, 80 DEG C is warming up under nitrogen protection, is completely dissolved benzoic acid;Then 10kg pairs is added in the reactor Toluenesulfonic acid is warming up to 115 DEG C, keeps the temperature 4 hours, reaction terminates, and obtains triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzene Formic acid esters;
2) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether, 130kg sulfamic acid and 70kg urea are added Enter in reactor;Stirring is started, is warming up to 115 DEG C under nitrogen protection, keeps the temperature 4 hours, reaction terminates, and obtains triphenylethylene base benzene Phenol polyethenoxy polyoxypropylene ether ammonium sulfate;
It 3) will be three made from triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether made from step 1, step 2 Styrylphenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate, isomery Tridecanol polyoxyethylene ether and water mix in proportion: triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether 22%, Triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate 12%, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate 12%, isomerous tridecanol polyoxyethylene ether 7%, surplus is water.Heating stirring is used for dacron to uniformly mixed to get one kind Oil removing level dyeing compound emulsifying agent.
Embodiment 4.
1) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether and 145kg benzoic acid are added to reactor In;Stirring is started, 80 DEG C is warming up under nitrogen protection, is completely dissolved benzoic acid;Then 9kg is added in the reactor to first Benzene sulfonic acid is warming up to 108 DEG C, keeps the temperature 4 hours, reaction terminates, and obtains triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzene first Acid esters;
2) 1200kg triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether, 125kg sulfamic acid and 65kg urea are added Enter in reactor;Stirring is started, is warming up to 112 DEG C under nitrogen protection, keeps the temperature 4 hours, reaction terminates, and obtains triphenylethylene base benzene Phenol polyethenoxy polyoxypropylene ether ammonium sulfate;
It 3) will be three made from triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether made from step 1, step 2 Styrylphenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate, isomery Tridecanol polyoxyethylene ether and water mix in proportion: triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether 8%, and three Styrylphenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate 12%, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate 11%, isomerous tridecanol polyoxyethylene ether 6%, surplus is water.Heating stirring is used for dacron to uniformly mixed to get one kind Oil removing level dyeing compound emulsifying agent.
Comparative example.
The property of the oil removing level dyeing compound emulsifying agent produced by the present invention for dacron is evaluated below by application test Can, wherein except oiliness test and market degreaser are the same as dosage comparison.Oil removing level dyeing compound emulsifying agent and the same dosage of market levelling agent Comparison carries out migration property test, slow metachromia test, defoaming test.
1. removing oiliness test
Oil removing level dyeing compound emulsifying agent/comparative sample degreaser 1g/L
Liquid alkaline (30%) 5g/L
Bath raio 1:10
Process flow: oilcloth obtained is cut into it is onesize spare, by above-mentioned formula prepare working solution, 98 DEG C heat preservation 30min, hot water wash, cold water are washed, drying, evaluation comparison.Effect assessment is referring to national standard GB/T 251-2008 " textile color stability Test evaluation staining gray scale ", staining gray scale is graded, and 5 grades of deoiling effect point, wherein 5 grades are best, 1 grade is most Difference.
2. migration property is tested
The cloth specimen that will be dyed with black ECT is dispersed cleans drying, takes dyeing terylene cloth specimen and the terylene cloth specimen that is unstained each 2.5g, it is stitched together, migration property test is carried out by following technological parameter:
Oil removing level dyeing compound emulsifying agent and comparative sample levelling agent are compared;Shifting is taken after washing drying by above-mentioned process The painting cloth after calico and shifting dye after dye tests cloth cover K/S value, calculates dye rate of moving, and shifting dye rate is calico K/S value and shifting after moving dye The ratio of painting cloth K/S value after dye;
3. slow metachromia test
According to following dyeing, cloth specimen is taken out when temperature reaches 90 DEG C, 110 DEG C respectively, wherein last block cloth specimen 80 DEG C of taking-ups are cooled to after 130 DEG C of heat preservation 30min, cloth specimen is dried after cleaning, and then tests cloth cover K/S value.
4. defoaming is tested
Reference standard GB/T21885-2008 " measurement of textile auxiliary's defoaming agent defoaming effect ", oil removing level dyeing is answered The solution of 10g/L is respectively configured in co-emulsifier and comparative sample levelling agent, pipettes 20ml at room temperature and has in plug graduated cylinder in 100ml, phase It is uniformly vibrated 20 times under the conditions of, stands observation, foam height at record 0 second, 1 minute is averaged for retest 3 times.
Experimental result:
1. removing oiliness
Remove oiliness of the present invention for the oil removing level dyeing compound emulsifying agent of dacron reaches market comparative sample degreaser Oil removing performance.
2. migration property
As can be seen from the above table, the migration property of oil removing level dyeing compound emulsifying agent is better than comparative sample levelling agent.
3. slow metachromia
The K/S value of test cloth specimen is as follows:
As can be seen from the table, the present invention is for the slow metachromia of the oil removing level dyeing compound emulsifying agent of dacron better than comparison Sample levelling agent, and cloth cover it is final color depth, illustrate oil removing level dyeing compound emulsifying agent wants small to the influence of the dye-uptake of dyestuff.
4. spumescence
As can be seen from the table, the present invention is obviously low for the foam height of the oil removing level dyeing compound emulsifying agent of dacron In comparative sample.
It is any ripe although the present invention is disclosed as above with embodiment, its protection scope being not intended to limit the invention The technical staff for knowing this technology changes and retouches made without departing from the spirit and scope of the invention, should belong to this The protection scope of invention.

Claims (4)

1. a kind of preparation method of the oil removing level dyeing compound emulsifying agent for dacron, which is characterized in that the preparation method Include the following steps:
(1) preparation of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether:
120 parts of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aethers and 13~15 parts of benzoic acid are added in reactor;It opens Dynamic stirring, is warming up to 80 DEG C under nitrogen protection, is completely dissolved benzoic acid;Then 0.7~1 part is added in the reactor to first Benzene sulfonic acid is warming up to 100~115 DEG C, keeps the temperature 3~4 hours, reaction terminates, and obtains triphenyl vinyl phenol polyoxyethylene polyoxy Propylene ester benzoic ether;
(2) preparation of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate:
120 parts of triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aethers, 11~13 parts of sulfamic acids and 5~7 parts of urea are added In reactor;Stirring is started, is warming up to 105~115 DEG C under nitrogen protection, keeps the temperature 3~4 hours, reaction terminates, and obtains triphen second Alkenyl benzene phenol polyethenoxy polyoxypropylene ether ammonium sulfate;
(3) triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether made from step (1), step (2) is obtained It is triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate, isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate, different Structure tridecanol polyoxyethylene ether 1309 and water mix in proportion, and heating stirring is knitted to get to one kind for terylene to uniformly mixed The oil removing level dyeing compound emulsifying agent of object;Wherein each component mass percentage are as follows: triphenyl vinyl phenol polyoxyethylene polyoxy third Alkene ester benzoic ether: 8~22%, triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate: 8~12%, isomery 13 Alcohol polyoxyethylene poly-oxygen propylene aether sodium sulphate: 8~12%, isomerous tridecanol polyoxyethylene ether 1309:3~7%, surplus is water.
2. the preparation method of the oil removing level dyeing compound emulsifying agent according to claim 1 for dacron, feature exist In the general formula of molecular structure of the triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether benzoic ether are as follows:
Wherein, m and n is integer;8≤m≤12,2≤n≤5.
3. the preparation method of the oil removing level dyeing compound emulsifying agent according to claim 1 for dacron, feature exist In the general formula of molecular structure of the triphenyl vinyl phenol polyoxyethylene poly-oxygen propylene aether ammonium sulfate are as follows:
Wherein, m and n is integer;8≤m≤12,2≤n≤5.
4. the preparation method of the oil removing level dyeing compound emulsifying agent according to claim 1 for dacron, feature exist In in the molecular structure of the isomerous tridecanol polyoxyethylene polyoxypropylene ether sodium sulfate, the number of oxyethylene group is 7~9, oxygen The number of acrylic is 1~3.
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CN112342801A (en) * 2020-10-27 2021-02-09 广东德美精细化工集团股份有限公司 High-temperature leveling agent for polyester superfine denier fabric and preparation method thereof
CN112724050A (en) * 2020-12-30 2021-04-30 武汉奥克特种化学有限公司 Phosphorus-free alkali-resistant solubilizer and preparation and application thereof

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CN107354778A (en) * 2017-06-23 2017-11-17 太仓大唐化纤厂 A kind of high-efficiency environment friendly high temperature levelling agent
CN107881811A (en) * 2017-12-26 2018-04-06 绍兴海成化工有限公司 A kind of multi-functional polyamide fibre dye leveller and preparation method thereof
CN107988795A (en) * 2016-10-26 2018-05-04 上海天坛助剂有限公司 A kind of environment-friendly multipurpose scouring agent and preparation method thereof

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CN107988795A (en) * 2016-10-26 2018-05-04 上海天坛助剂有限公司 A kind of environment-friendly multipurpose scouring agent and preparation method thereof
CN106555342A (en) * 2016-12-01 2017-04-05 淄博大染坊丝绸集团有限公司 A kind of reactive disperse dyes one bathes polyester cotton blended yarn dyeing
CN107354778A (en) * 2017-06-23 2017-11-17 太仓大唐化纤厂 A kind of high-efficiency environment friendly high temperature levelling agent
CN107881811A (en) * 2017-12-26 2018-04-06 绍兴海成化工有限公司 A kind of multi-functional polyamide fibre dye leveller and preparation method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112342801A (en) * 2020-10-27 2021-02-09 广东德美精细化工集团股份有限公司 High-temperature leveling agent for polyester superfine denier fabric and preparation method thereof
CN112724050A (en) * 2020-12-30 2021-04-30 武汉奥克特种化学有限公司 Phosphorus-free alkali-resistant solubilizer and preparation and application thereof

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