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CN106638054A - Terylene reduction cleaning agent and preparation method thereof - Google Patents

Terylene reduction cleaning agent and preparation method thereof Download PDF

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Publication number
CN106638054A
CN106638054A CN201610905881.0A CN201610905881A CN106638054A CN 106638054 A CN106638054 A CN 106638054A CN 201610905881 A CN201610905881 A CN 201610905881A CN 106638054 A CN106638054 A CN 106638054A
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Prior art keywords
reduction
terylene
proportion
parts
mixes
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CN201610905881.0A
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CN106638054B (en
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余云义
杨中新
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Transfar Forland Fine Chemicals Foshan Co Ltd
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Transfar Forland Fine Chemicals Foshan 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
    • D06P5/00Other features in dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form
    • D06P5/02After-treatment
    • D06P5/04After-treatment with organic compounds
    • 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
    • D06P5/00Other features in dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form
    • D06P5/02After-treatment
    • D06P5/04After-treatment with organic compounds
    • D06P5/08After-treatment with organic compounds macromolecular
    • 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
    • D06P5/00Other features in dyeing or printing textiles, or dyeing leather, furs, or solid macromolecular substances in any form
    • D06P5/02After-treatment
    • D06P5/10After-treatment with compounds containing metal

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Detergent Compositions (AREA)

Abstract

The invention discloses a reduction cleaning agent for terylene. The reduction cleaning agent for the terylene is characterized by comprising deionized water, an unsaturated reduction system, a surfactant system and a pH value buffering system, in parts by mass: 84 to 35 parts of the deionized water, 10 to 50 parts of the unsaturated reduction system, 5 to 10 parts of the surfactant system and 1 to 5 parts of the pH value buffering system. The reduction cleaning agent for the terylene is stable in state, avoids heating and spontaneous combustion conditions, does not have pungent smell, is convenient to transport and store, and has an excellent cleaning effect.

Description

A kind of terylene reduction cleaner and preparation method thereof
Technical field
The present invention relates to fabric finishing auxiliary agent field, the specifically a kind of replacement sodium hydrosulfite and good terylene of cleaning performance is also Former cleaning agent and preparation method thereof.
Background technology
Terylene is the one kind in synthetic fibers, because its own has extremely outstanding shaping performance, in experience repeatedly washing Afterwards the anti-deformation nature of terylene is still very excellent, so it is widely used in the industries such as clothing, weaving.And as fabric is mixed The continuous development of spinning technique, the fabric of polyester cotton blending is increasingly favored by clothing producer.Although terylene has and excellent determines Type performance, but it adds man-hour to there is a great technological deficiency in dyeing and finishing.Traditional terylene is carried out using disperse dyes mostly Dyeing, and disperse dyes belong to nonpolar small molecule, its hydrophilicity extreme difference, so at all cannot be using normal in terylene dyeing and finishing The washing means of rule remove the loose colour of web surface.Traditional method is using sodium dithionite (being commonly called as sodium hydrosulfite) and burns The alkali or soda ash isothermal holding 20-30 minutes more than 85 DEG C, to solve the problems, such as that disperse dyes polarity is too low washing is difficult to.So And, sodium dithionite be both have strong reducing property, it may have the unstable material of strong oxidizing property, be heated, make moist it is even sudden and violent Being exposed in air can all cause the fast decoupled even spontaneous combustion of sodium dithionite, thus sodium dithionite must it is special, Store under independent environment, the security extreme difference that it is used.Meanwhile, sodium dithionite has intense irritation smell, to people Body health has very big harm, and when carrying out reduction cleaning using sodium dithionite and soda ash, it is intractable except easily producing Outside sewage, fabric also needs to a large amount of clear water and is rinsed, and is added significantly to the dirt of the energy consumption and emission of fabric finishing to environment Dye.Additionally, fabric also needs to add acid to be neutralized reaction after washing, so as to cause the waste of various resources.
In order to solve the above problems, occur in that the reduction of disperse dyes based on thiourea dioxide is clear in the market Lotion.Thiourea dioxide has stronger reproducibility, relatively stable in an acidic solution, but in the basic conditions it is easy to point Solution, generates the very strong sulfinic acid of reproducibility.Although thiourea dioxide stability increases compared with sodium dithionite, it is being deposited Protection against the tide, solar heat protection are still needed when putting and sunlight direct irradiation is avoided, and the penetrating odor that its decomposition is produced is more or less residual On the product stayed in after reduction cleaning.
The document and patent report mistake of external early stage, improvement is proposed surely for the reducing agent of reduction cleaning after dispersion dyeing Qualitatively method, such as publication number:Propose to adopt in the american documentation literature of USP2516321 to be mixed into 3-10 part solid sodium pyroborates With the mixture of 3-10 part solid polyformaldehydes to improve the stability that solid-state connects sodium sulfite, but due to connecting depositing for sodium sulfite , still must be moistureproof during its storage and avoid amount of heat from affecting, and the free of formaldehyde makes its residual quantity can be well beyond REACH methods The standard of the free formaldehyde content control for then specifying.
And publication number:Using the C of addition 0.5-45% percentage by weights in the american documentation literature of USP30546581-18Chain Alkanoic acid sodium salt;Publication number:Such as sodium chloride, sodium sulphate and sodium phosphate are then adopted in the american documentation literature of USP2707144, it is special It is not the anhydrous inorganic salts and even sodium sulfite mixture of sodium polyphosphate, it is with the company's of raising sodium sulfite heat endurance but aforementioned Introducing the mode of additive can not at all solve the problems, such as that powdery connects heat release spontaneous combustion after sodium sulfite moisture regain, and it is met and still can go out after water Now decompose and discharge the phenomenon of sulfide rapidly.
In publication number:Oxalic acid, borate and water-soluble inorganic carbonate are then adopted in USP3669895 american documentation literatures The mode of mixture addition, even sodium sulfite runs into the temperature that the heat produced during moisture is less than spontaneous combustion, wherein Boratex for control Can further improve reduction efficiency.But, it is situations such as the moisture and the globule that dyeing and printing process factory produces in dyeing and finishing process is sputtered What processor cannot predict at all, once atmospheric water content can still cause enough powdery to connect sodium sulfite generation heat reach Or more than autoignition temperature.
And publication number:Although the solid particle stabilising system illustrated in american documentation literature 4066390 contaminates in disperse dyes Good cleaning performance can be obtained after color, but it still falls within solid-like, uses and operation is inconvenient;Secondly, when solid mixes Environment and processing conditions can all cause the problem of its less stable.Furthermore the situation of airborne dust easily occurs in solid particle, cause behaviour Author sucks and causes respiratory tract occupational disease.
From the above it can be seen that at present the reduction cleaning system of terylene remains many critical defects.
The content of the invention
It is an object of the invention to overcome the deficiencies in the prior art, there is provided one kind is in stable condition, be not in heating and oneself The terylene reduction cleaner of condition of lighting the passion.
Another object of the present invention is to overcome the deficiencies in the prior art, there is provided one kind has no irritating odor, is readily transported With store and possess the terylene reduction cleaner of excellent cleaning performance.
Another object of the present invention is to provide a kind of method for preparing above-mentioned terylene reduction cleaner of process is simple.
What the goal of the invention of the present invention was realized in:A kind of terylene reduction cleaner, it is characterised in that:The terylene Include deionized water, unsaturated reduction system, surfactant system and pH value buffer system, said components with reduction cleaner It is respectively by mass fraction:Deionized water 84-35 part, unsaturated reduction system 10-50 parts, surfactant system 5-10 Part, pH value buffer system 1-5 part.
Furtherly, the unsaturated reduction system includes main reduction components and secondary reduction components, main reduction components and pair The mol ratio of reduction components is (1-50):1.
Furtherly, main reduction components include isomery polyalcohol or isomery polyaldehyde or the two mixture, its Following one kind is included at least in molecular structure:
N is 1-100 in above-mentioned molecular structure, R1, R2, R3, R4 be respectively hydrogen, carbon number for the straight chain between 1-6 or At least one in branched alkyl and phenyl ring, X is CH2OH or CH2At least one in O.
Furtherly, secondary reduction components include the one kind in sulfur-bearing reducing compound, non-steady state halogen and boron hydrogen salt Or mix in any proportion.
Furtherly, sulfur-bearing reducing compound is included in sulphite, sodium thiosulfate, akali sulphide and NaHS One kind mixes in any proportion.
Furtherly, non-steady state halogen is including the one kind in frerrous chloride and protochloride zinc or mixes in any proportion Close.
Furtherly, boron hydrogen salt is including the one kind in sodium borohydride and potassium borohydride or mixes in any proportion.
Furtherly, surfactant includes that anion surfactant and nonionic surfactant are mixed with arbitrary proportion Close.
Furtherly, anion surfactant includes alkylbenzenesulfonate, alkyl sulfate, APEO sulfuric acid One kind in ester, polyoxyethylene ether phosphate mixes in any proportion.
Furtherly, nonionic surfactant is included in alkyl alcohol ethoxylates and aliphatic amine polyoxyethylene ether One kind mixes in any proportion.
Furtherly, pH value buffer system is including the one kind in organic/inorganic weak acid and organic/inorganic weak base or by any Ratio mixes, and the pH value range of pH value buffer system is 5-9.
Furtherly, pH value buffer system is the mixture of phosphate and sodium acetate or phosphate and sodium carbonate.
Furtherly, pH value buffer system is the mixture of phosphate and monoethanolamine or phosphate and diethylenetriamine.
The step of present invention also provides a kind of method for preparing above-mentioned terylene reduction cleaner, the method is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, water and pH are sequentially added in the sealing container with mixer, stirred Minute time 5-20;
c:Temperature in the container of b step is maintained to be normal temperature and pressure, under lasting stirring toward mixture obtained by b step Surfactant is added, then temperature in container 50-100 DEG C is promoted to, and 10-50 is incubated under lasting stirring and divided Clock;
d:Temperature in step c container is reduced to 30-60 DEG C, is added toward mixture obtained by step c under lasting stirring Enter unsaturated reducing agent, and terylene reduction cleaner is obtained by being incubated 10-50 minutes under lasting stirring.
The present invention is improved to the terylene reduction cleaner of prior art, and its advantage is as follows:
1st, in terylene reduction cleaner of the invention, the compounding reduction group of main reduction components and secondary reduction system is employed Point.Wherein main reduction components include isomery polyalcohol or isomery polyaldehyde, and secondary reduction components include sulfur-bearing reducing compound, non-steady Stationary state halogen and boron hydrogen salt.First, main reduction components itself have stronger reproducibility, and it can be to the unstable reduction of solid-state Component produces stronger organic dissolution effect, intercepts the contact of unstable reduction components and the external world, it is to avoid it oxidation Decomposition occurs Situation, use and the stability that stores and reliability so as to reduction cleaner greatly improved.Simultaneously main reduction components are utilized The reproducibility of its own can effectively destroy in disperse dyes chromonic structure in terylene reduction cleaning or tie dye molecule Structure is decomposed reaction, makes dye molecule come off from terylene or bafta, so as to reach the purpose fully stripped.Secondly, it is secondary Reduction components can produce collaborative SCM effect during whole reduction cleaning, between main reducing agent, can reduce going back for fabric Former current potential, and improve the reducing power of main reduction components, so as to greatly improve stripping of the reduction cleaner to dye molecule on fabric From ability.Additionally, the compound system of main reduction components and secondary reduction components is not in when in use the situation of decomposition, thus not Fuel gas or corrosive gas can be produced.Meanwhile, the compound system will not also produce penetrating odor in dyeing and finishing process, and Residue will not be formed on fabric.
2nd, in terylene reduction cleaner of the invention, the surfactant system of Compositional type is added.First, surface-active System makes detergent solution align in the surface formation of dye particles, and significantly reduces between cleaning agent and dye particles Surface tension, so that cleaning agent particle can fully infiltrate dye particles, improves stripping energy of the cleaning agent particle to dye particles Power.Secondly, nonionic surfactant does not produce in the solution ionization, and it is difficult to be affected by dielectric, so can effectively carry The stability of high surface system.Finally, hydrophilic anions can be in the solution formed after anion surfactant dissolving, It can form infiltration film body by way of foam, and into the gap between liquid phase and solid phase, improve cleaning agent to dyestuff grain Son wetting capacity, so as to improve its free state dye particles to fabric face separating power and fabric fastness to washing and Crock fastness.
3rd, in terylene reduction cleaner of the invention, adding can stablize the pH value buffering group of reduction cleaning system pH Point.By pH value buffer components disengaging in cleaning system, the pH value change occurred in cleaning process can be effectively hindered, be made Reduction cleaning system is in all the time under stable reduction reaction environment, so as to ensure that being smoothed out for terylene reduction cleaning.
4th, terylene reduction cleaner of the invention is prepared using the mixing method that mixes.First, the mixing method that mixes can be improved The uniformity of reduction cleaning agent solution so as to possess stable chemical reactivity, and make main reduction components and secondary reduction components All the time under stable reactiveness, the chemical stability of cleaning system has been ensured.Secondly, the process of the mixing method that mixes is very Simply, the preparation difficulty of reduction cleaner can be effectively reduced, its preparation time is reduced, and production process is easily controlled, during preparation Also penetrating odor will not be produced, therefore can effectively reduces the preparation cost of cleaning agent.
Specific embodiment
The terylene of present invention reduction cleaner mainly includes deionized water, unsaturated reducing agent, surfactant and pH Value buffer, said components are respectively by mass fraction:Deionized water 84-35 part, unsaturated reduction system 10-50 parts, table Surfactant system 5-10 parts, pH value buffer system 1-5 part.Wherein, unsaturated reduction system includes main reduction components and pair also The mol ratio of stock blend, main reduction components and secondary reduction components is (1-50):1.By main reduction components and secondary reduction components structure Into compounding reduction system, make reducing agent form the storage environment of solution-type, unstable reducing substances is prevented effectively from and the external world Air contact, it is to avoid its situation for oxidation deterioration occur or decomposing spontaneous combustion, the storage of effective guarantee reduction system and reaction Stability agent reliability.Meanwhile, synergy of the reduction system using major and minor reduction components is compounded, promote reducing agent to fabric The free state dye particles on surface are peeled off, and improve speed and efficiency that dye molecule comes off from terylene or bafta.
The main reduction components of the present invention employ isomery polyalcohol or isomery polyaldehyde or the two mixture, According to the species of dyestuff, isomery polyalcohol and isomery polyaldehyde can be used alone or be used in mixed way when actually used. Following one kind is included at least in its molecular structure:
In above-mentioned molecular structure, n is 1-100, and R1, R2, R3, R4 are respectively hydrogen, carbon number for the straight chain between 1-6 or prop up At least one in alkyl group, phenyl ring, X is CH2OH or CH2At least one in O.In structure A and structure B, straight chain is employed The reactive group arrangement mode of type, straight chain type arrangement can ensure that reducing agent is carried out with the free state dye particles on dacron Fully reaction, improves the speed of reduction reaction.And in structure C, D, E, then employ radial reactive group arrangement Mode, radial arrangement can ensure free state dye particles on reducing agent and dacron being fully contacted spatially, carry The high efficiency of reduction reaction.
The present invention secondary reduction components can adopt sulfur-bearing reducing compound, non-steady state halogen and boron hydrogen salt in one kind or Mix in any proportion.Wherein, sulfur-bearing reducing compound is using in sulphite, sodium thiosulfate, akali sulphide and NaHS One kind or mix in any proportion;And non-steady state halogen is using the one kind in frerrous chloride and protochloride zinc or by arbitrarily ratio Example mixing;Boron hydrogen salt then mixes using the one kind in sodium borohydride and potassium borohydride or in any proportion.Sulfur-bearing reducing compound Itself has stronger reduction reaction ability, and it is dissolved in alcohol or aldehyde solution, and has in reduction system very strong Collaborative SCM is acted on, and can promote stripping of the dye particles on fabric.Non-steady state halogen then has stronger suction-operated, energy Effectively improve absorption efficiency of the dye particles after fabric is peeled off, it is to avoid the generation of secondary pollution on fabric.Boron hydrogen salt except Possess outside reduction reaction ability, its stability in air and water is stronger, and it has more flexible reaction selectivity, can protect Stablizing for reduction reaction is carried out barrier.
It is mixed with arbitrary proportion that the surfactant of the present invention adopts anion surfactant and nonionic surfactant Close.Wherein, anion surfactant employs alkylbenzenesulfonate, alkyl sulfate, ethylene oxide ether sulfate, polyoxy second One kind in alkene ether phosphate mixes in any proportion.And nonionic surfactant then employs alkyl alcohol ethoxylates With the one kind in aliphatic amine polyoxyethylene ether or mix in any proportion.First, nonionic surfactant is not produced in the solution Raw ionization, it is difficult to be affected by dielectric, so the stability of surface active system can be effectively improved.Secondly, anion table Infiltration film body can be formed by way of foam after the activating agent dissolving of face, improves wetting capacity of the cleaning agent to dye particles, from And improve the separating power of its free state dye particles to fabric face and fastness to washing, the crock fastness of fabric.
The pH value buffer system of the present invention is using the one kind in organic/inorganic weak acid and organic/inorganic weak base or by any Ratio mixes, in order to ensure being smoothed out for reduction reaction, for the pH value model of pH value buffer system under different dyeing and finishing environment Enclose and may be set to 5-9.The pH value buffer system of the present invention can adopt the mixing of phosphate and sodium acetate or phosphate and sodium carbonate Thing, or the mixture of phosphate and monoethanolamine or phosphate and diethylenetriamine.First, phosphate itself has stronger Reactivity, in reaction weak acid can be disengaged, and it belongs to biological state material, adding man-hour to reduce reduction system to environment Pollution.Secondly, sodium acetate and sodium carbonate then have upon dissolution stronger alkalescence, but it is to its neutralization adjustment effect of pH value.Most Afterwards, monoethanolamine and diethylenetriamine are likewise supplied with stronger alkalescence in reduction system, and due to monoethanolamine and divinyl three Amine belongs to organic base, and reactive group can also be provided for reduction system while pH value is adjusted.
The step of present invention also provides a kind of method for preparing above-mentioned terylene reduction cleaner, the method is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, water and pH are sequentially added in the sealing container with mixer, stirred Minute time 5-20;
c:Temperature in the container of b step is maintained to be normal temperature and pressure, under lasting stirring toward mixture obtained by b step Surfactant is added, then temperature in container 50-100 DEG C is promoted to, and 10-50 is incubated under lasting stirring and divided Clock;
d:Temperature in step c container is reduced to 30-60 DEG C, is added toward mixture obtained by step c under lasting stirring Enter unsaturated reducing agent, and terylene reduction cleaner is obtained by being incubated 10-50 minutes under lasting stirring.
Present disclosure is described further with reference to specific embodiment, but is not therefore limited the invention to In the scope of embodiments:
Embodiment 1
The terylene of the present invention includes deionized water, main reduction components, sulphite, alkyl benzene sulphonate with reduction cleaner The mixture of salt, alkyl alcohol ethoxylates, phosphate and sodium acetate.Wherein, main reduction components be isomery polyalcohol, its molecule Structure is:
N is 1 in above-mentioned molecular structure, and R1, R2 are respectively the alkyl that hydrogen, carbon number are 1.Main reducing agent rubs with secondary reducing agent You are than being 4:1, and pH value is controlled 5.Said components are respectively by mass fraction:84 parts of deionized water, isomery polyalcohol 8 Part, 2 parts of sulphite, 3 parts of alkylbenzenesulfonate, 2 parts of alkyl alcohol ethoxylates, 0.5 part of phosphate, 0.5 part of sodium acetate.
The step of preparation method of above-mentioned terylene reduction cleaner, is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, water and pH are sequentially added in the sealing container with mixer, stirred 5 minutes time;
c:Temperature in the container of b step is maintained to be normal temperature and pressure, under lasting stirring toward mixture obtained by b step Surfactant is added, then temperature in container 50 DEG C is promoted to, and 10 minutes are incubated under lasting stirring;
d:Temperature in step c container is reduced to 30 DEG C, is added not toward mixture obtained by step c under lasting stirring Saturation reducing agent, and terylene reduction cleaner 1 is obtained by being incubated 10 minutes under lasting stirring.
Embodiment 2
The present invention terylene with reduction cleaner include deionized water, main reduction components, sulphite, sodium thiosulfate, Akali sulphide, NaHS, frerrous chloride, protochloride zinc, sodium borohydride, potassium borohydride, alkylbenzenesulfonate, alkyl sulfate, Ethylene oxide ether sulfate, polyoxyethylene ether phosphate, alkyl alcohol ethoxylates, aliphatic amine polyoxyethylene ether, phosphate and The mixture of monoethanolamine.Wherein, main reduction components are the mixture of isomery polyalcohol and isomery polyaldehyde, and its molecular structure is:
N is 100 in above-mentioned molecular structure, and R3, R4 are respectively the straight chained alkyl and phenyl ring that carbon number is 6, and X is CH2OH。 The mol ratio of main reducing agent and secondary reducing agent is 11:1, and pH value is controlled 9.Said components are respectively by mass fraction:Go 35 parts of ionized water, 20 parts of isomery polyalcohol, 20 parts of isomery polyaldehyde, 1 part of sulphite, 1 part of sodium thiosulfate, 2 parts of akali sulphide, 1 part of NaHS, 2 parts of frerrous chloride, 1 part of protochloride zinc, 1 part of sodium borohydride, 1 part of potassium borohydride, 3 parts of alkylbenzenesulfonate, 2 parts of alkyl sulfate, 2 parts of ethylene oxide ether sulfate, 1 part of polyoxyethylene ether phosphate, 1 part of alkyl alcohol ethoxylates, fat 1 part of fat amine APEO, 2 parts of phosphate, 3 parts of monoethanolamine.
The step of preparation method of above-mentioned terylene reduction cleaner, is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, water and pH are sequentially added in the sealing container with mixer, stirred 20 minutes time;
c:Temperature in the container of b step is maintained to be normal temperature and pressure, under lasting stirring toward mixture obtained by b step Surfactant is added, then temperature in container 100 DEG C is promoted to, and 50 minutes are incubated under lasting stirring;
d:Temperature in step c container is reduced to 60 DEG C, is added not toward mixture obtained by step c under lasting stirring Saturation reducing agent, and terylene reduction cleaner 2 is obtained by being incubated 50 minutes under lasting stirring.
Embodiment 3
The terylene of the present invention includes deionized water, main reduction components, sodium thiosulfate, akali sulphide, sulphur with reduction cleaner Sodium hydride, alkyl sulfate, ethylene oxide ether sulfate, polyoxyethylene ether phosphate, aliphatic amine polyoxyethylene ether, phosphate and The mixture of sodium carbonate.Wherein, main reduction components are isomery polyaldehyde, and its molecular structure is:
X is CH in above-mentioned molecular structure2O.The mol ratio of main reducing agent and secondary reducing agent is 4:1, and pH value is controlled 6.It is above-mentioned Component is respectively by mass fraction:63 parts of deionized water, 20 parts of isomery polyaldehyde, 1 part of sodium thiosulfate, 1 part of akali sulphide, sulphur 3 parts of sodium hydride, 3 parts of alkyl sulfate, 2 parts of ethylene oxide ether sulfate, 3 parts of polyoxyethylene ether phosphate, fatty amine polyoxy second 2 parts of alkene ether, 1 part of phosphate, 1 part of sodium carbonate.
The step of preparation method of above-mentioned terylene reduction cleaner, is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, water and pH are sequentially added in the sealing container with mixer, stirred 10 minutes time;
c:Temperature in the container of b step is maintained to be normal temperature and pressure, under lasting stirring toward mixture obtained by b step Surfactant is added, then temperature in container 65 DEG C is promoted to, and 20 minutes are incubated under lasting stirring;
d:Temperature in step c container is reduced to 35 DEG C, is added not toward mixture obtained by step c under lasting stirring Saturation reducing agent, and terylene reduction cleaner 3 is obtained by being incubated 20 minutes under lasting stirring.
Embodiment 4
The terylene of the present invention includes deionized water, main reduction components, frerrous chloride, protochloride zinc, boron with reduction cleaner Sodium hydride, potassium borohydride, alkylbenzenesulfonate, alkyl sulfate, ethylene oxide ether sulfate, polyoxyethylene ether phosphate, alkane The mixture of base alcohol APEO, aliphatic amine polyoxyethylene ether, phosphate and sodium acetate.Wherein, main reduction components are isomery The mixture of polyalcohol and isomery polyaldehyde, its molecular structure is:
N is 40 in above-mentioned molecular structure, and R1, R2 are respectively the branched alkyl that hydrogen, carbon number are 5, and X is CH2O.Main reducing agent It is 6 with the mol ratio of secondary reducing agent:1, and pH value is controlled 7.5.Said components are respectively by mass fraction:Deionized water 52 Part, 15 parts of isomery polyalcohol, 15 parts of isomery polyaldehyde, 1 part of frerrous chloride, 2 parts of protochloride zinc, 1 part of sodium borohydride, potassium borohydride 1 part, 2 parts of alkylbenzenesulfonate, 2 parts of alkyl sulfate, 1 part of ethylene oxide ether sulfate, 2 parts of polyoxyethylene ether phosphate, alkane 2 parts of base alcohol APEO, 1 part of aliphatic amine polyoxyethylene ether, 2 parts of phosphate, 1 part of sodium acetate.
The step of preparation method of above-mentioned terylene reduction cleaner, is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, water and pH are sequentially added in the sealing container with mixer, stirred 15 minutes time;
c:Temperature in the container of b step is maintained to be normal temperature and pressure, under lasting stirring toward mixture obtained by b step Surfactant is added, then temperature in container 75 DEG C is promoted to, and 30 minutes are incubated under lasting stirring;
d:Temperature in step c container is reduced to 45 DEG C, is added not toward mixture obtained by step c under lasting stirring Saturation reducing agent, and terylene reduction cleaner 4 is obtained by being incubated 30 minutes under lasting stirring.
Embodiment 5
The present invention terylene with reduction cleaner include deionized water, main reduction components, sulphite, sodium thiosulfate, Akali sulphide, frerrous chloride, sodium borohydride, alkylbenzenesulfonate, alkyl sulfate, ethylene oxide ether sulfate, APEO The mixture of phosphate, alkyl alcohol ethoxylates, aliphatic amine polyoxyethylene ether, phosphate and diethylenetriamine.Wherein, it is main to go back Stock blend is the mixture of isomery polyalcohol and isomery polyaldehyde, and its molecular structure is:
N is 60 in above-mentioned molecular structure, and it is the straight chained alkyl between 5 that R3, R4 are respectively hydrogen, carbon number, and X is CH2OH.It is main to go back The mol ratio of former agent and secondary reducing agent is 8:1, and pH value is controlled 8.Said components are respectively by mass fraction:Deionized water 40 parts, 20 parts of isomery polyalcohol, 20 parts of isomery polyaldehyde, 1 part of sulphite, 1 part of sodium thiosulfate, 1 part of akali sulphide, protochloride 1 part of iron, 1 part of sodium borohydride, 2 parts of alkylbenzenesulfonate, 1 part of alkyl sulfate, 2 parts of ethylene oxide ether sulfate, polyoxyethylene 2 parts of ether phosphate, 1 part of alkyl alcohol ethoxylates, 2 parts of aliphatic amine polyoxyethylene ether, 2 parts of phosphate, 3 parts of diethylenetriamine.
The step of preparation method of above-mentioned terylene reduction cleaner, is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, water and pH are sequentially added in the sealing container with mixer, stirred 18 minutes time;
c:Temperature in the container of b step is maintained to be normal temperature and pressure, under lasting stirring toward mixture obtained by b step Surfactant is added, then temperature in container 85 DEG C is promoted to, and 40 minutes are incubated under lasting stirring;
d:Temperature in step c container is reduced to 55 DEG C, is added not toward mixture obtained by step c under lasting stirring Saturation reducing agent, and terylene reduction cleaner 5 is obtained by being incubated 40 minutes under lasting stirring.
By terylene reduction cleaner 1-5 obtained in above-described embodiment 1-5, performance test is carried out, method of testing is as follows:
(1) dacron is dyeed using HTHP machine, dye strength 5%, cooling, washing after dye;
(2) reduction cleaner or sodium hydrosulfite of 2g/L are added, the caustic soda of 2g/L is acted on 20 minutes at 85 DEG C, finally right Fabric is washed, is dried;
(3) discoloration, wash water fastness and the staining fastness of fabric are determined using GB/T 251-1995, using GB/T 3920-1997 crock fastness for determining fabric.
The results are shown in Table 1:
Table 1 carries out the fastness ability after reduction cleaning using embodiment 1-5 and sodium hydrosulfite

Claims (10)

1. a kind of terylene reduction cleaner, it is characterised in that:The terylene includes deionized water, unsaturation with reduction cleaner Reduction system, surfactant system and pH value buffer system, said components are respectively by mass fraction:Deionized water 84- 35 parts, unsaturated reduction system 10-50 parts, surfactant system 5-10 parts, pH value buffer system 1-5 part.
2. terylene reduction cleaner according to claim 1, it is characterised in that:The unsaturated reduction system includes main going back The mol ratio of stock blend and secondary reduction components, main reduction components and secondary reduction components is (1-50):1.
3. terylene reduction cleaner according to claim 2, it is characterised in that:The main reduction components include that isomery is polynary Alcohol or isomery polyaldehyde or the two mixture, include at least following one kind in its molecular structure:
N is 1-100 in above-mentioned molecular structure, and R1, R2, R3, R4 are respectively hydrogen, carbon number for the straight or branched between 1-6 At least one in alkyl and phenyl ring, X is CH2OH or CH2At least one in O.
4. terylene reduction cleaner according to claim 2, it is characterised in that:The secondary reduction components are reduced including sulfur-bearing One kind in compound, non-steady state halogen and boron hydrogen salt mixes in any proportion.
5. terylene reduction cleaner according to claim 4, it is characterised in that:The sulfur-bearing reducing compound includes sulfurous One kind in hydrochlorate, sodium thiosulfate, akali sulphide and NaHS mixes in any proportion.
6. terylene reduction cleaner according to claim 4, it is characterised in that:The non-steady state halogen includes protochloride One kind in iron and protochloride zinc mixes in any proportion.
7. terylene reduction cleaner according to claim 4, it is characterised in that:The boron hydrogen salt includes sodium borohydride and boron One kind in hydrofining mixes in any proportion.
8. terylene reduction cleaner according to claim 1, it is characterised in that:The surfactant includes anion table , with arbitrary proportion mixing, the anion surfactant includes alkyl benzene sulphonate for face activating agent and nonionic surfactant One kind in salt, alkyl sulfate, ethylene oxide ether sulfate, polyoxyethylene ether phosphate mixes in any proportion, described Nonionic surfactant includes the one kind in alkyl alcohol ethoxylates and aliphatic amine polyoxyethylene ether or mixes in any proportion Close.
9. terylene reduction cleaner according to claim 1, it is characterised in that:The pH value buffer system include it is organic/ One kind in inorganic weak acid and organic/inorganic weak base mixes in any proportion, and the pH value range of pH value buffer system is 5-9,
The pH value buffer system is the mixture of phosphate and sodium acetate or phosphate and sodium carbonate;
Or the mixture that the pH value buffer system is phosphate and monoethanolamine or phosphate and diethylenetriamine.
10. a kind of preparation method of the reduction cleaner of terylene according to claim 1, it is characterised in that:The preparation side The step of method, is as follows:
a:Corresponding raw material for standby is weighed according to said ratio;
b:Under normal temperature and pressure state, in the sealing container with mixer water and pH, mixing time are sequentially added 5-20 minutes;
c:Maintain temperature in the container of b step to be normal temperature and pressure, add toward mixture obtained by b step under lasting stirring Surfactant, is then promoted to 50-100 DEG C temperature in container, and is incubated 10-50 minutes under lasting stirring;
d:Temperature in step c container is reduced to 30-60 DEG C, is added not toward mixture obtained by step c under lasting stirring Saturation reducing agent, and terylene reduction cleaner is obtained by being incubated 10-50 minutes under lasting stirring.
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Cited By (5)

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CN107723118A (en) * 2017-09-21 2018-02-23 无锡德冠生物科技有限公司 A kind of acidic reduction cleaner and preparation method thereof
CN107938398A (en) * 2017-11-14 2018-04-20 五邑大学 A kind of oxalic acid rongalite combination of acidic reduction cleaner, its preparation method and its application
CN107956171A (en) * 2017-11-14 2018-04-24 五邑大学 A kind of vulcanized sodium rongalite combination of acidic reduction cleaner, its preparation method and its application
CN108071029A (en) * 2017-11-14 2018-05-25 五邑大学 A kind of sodium thiosulfate rongalite combination of acidic reduction cleaner, its preparation method and its application
CN110512443A (en) * 2019-10-10 2019-11-29 如意屋家居有限公司 A method of it is cross-linked into film preparation by padding and removes peculiar smell curtain

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CN104652143A (en) * 2015-02-10 2015-05-27 浙江工业职业技术学院 Reductive cleansing agent and preparation method thereof
CN105714585A (en) * 2016-04-12 2016-06-29 张家港市德宝化工有限公司 Reductive cleaning agent for synthetic fibers as well as preparation method and application of reductive cleaning agent

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CN102808340A (en) * 2012-08-21 2012-12-05 义乌市中力工贸有限公司 Stable liquid reductive cleaner after disperse dyeing
CN104652143A (en) * 2015-02-10 2015-05-27 浙江工业职业技术学院 Reductive cleansing agent and preparation method thereof
CN105714585A (en) * 2016-04-12 2016-06-29 张家港市德宝化工有限公司 Reductive cleaning agent for synthetic fibers as well as preparation method and application of reductive cleaning agent

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107723118A (en) * 2017-09-21 2018-02-23 无锡德冠生物科技有限公司 A kind of acidic reduction cleaner and preparation method thereof
CN107938398A (en) * 2017-11-14 2018-04-20 五邑大学 A kind of oxalic acid rongalite combination of acidic reduction cleaner, its preparation method and its application
CN107956171A (en) * 2017-11-14 2018-04-24 五邑大学 A kind of vulcanized sodium rongalite combination of acidic reduction cleaner, its preparation method and its application
CN108071029A (en) * 2017-11-14 2018-05-25 五邑大学 A kind of sodium thiosulfate rongalite combination of acidic reduction cleaner, its preparation method and its application
CN110512443A (en) * 2019-10-10 2019-11-29 如意屋家居有限公司 A method of it is cross-linked into film preparation by padding and removes peculiar smell curtain
CN110512443B (en) * 2019-10-10 2021-12-31 如意屋家居有限公司 Method for preparing peculiar smell removing curtain by padding and crosslinking film forming

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