CN116376647A - Bio-based polyester degreasing agent as well as preparation method and application thereof - Google Patents

Bio-based polyester degreasing agent as well as preparation method and application thereof Download PDF

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Publication number
CN116376647A
CN116376647A CN202310015705.XA CN202310015705A CN116376647A CN 116376647 A CN116376647 A CN 116376647A CN 202310015705 A CN202310015705 A CN 202310015705A CN 116376647 A CN116376647 A CN 116376647A
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degreasing agent
polyester
bio
oil
degreasing
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Inventor
储鑫
徐有琦
华燕
刘建乐
黄婧
邹峰
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Wuxi Colotex Bio Technology Co ltd
Jiangsu New Reba Technology Co ltd
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Wuxi Colotex Bio Technology Co ltd
Jiangsu New Reba Technology Co ltd
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/37Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/53Polyethers
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D10/00Compositions of detergents, not provided for by one single preceding group
    • C11D10/04Compositions of detergents, not provided for by one single preceding group based on mixtures of surface-active non-soap compounds and soap
    • C11D10/042Compositions of detergents, not provided for by one single preceding group based on mixtures of surface-active non-soap compounds and soap based on anionic surface-active compounds and soap
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11DDETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
    • C11D10/00Compositions of detergents, not provided for by one single preceding group
    • C11D10/04Compositions of detergents, not provided for by one single preceding group based on mixtures of surface-active non-soap compounds and soap
    • C11D10/045Compositions of detergents, not provided for by one single preceding group based on mixtures of surface-active non-soap compounds and soap based on non-ionic surface-active compounds and soap
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M13/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
    • D06M13/10Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing oxygen
    • D06M13/184Carboxylic acids; Anhydrides, halides or salts thereof
    • D06M13/207Substituted carboxylic acids, e.g. by hydroxy or keto groups; Anhydrides, halides or salts thereof
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M13/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
    • D06M13/244Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing sulfur or phosphorus
    • D06M13/248Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing sulfur or phosphorus with compounds containing sulfur
    • D06M13/256Sulfonated compounds esters thereof, e.g. sultones
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M13/00Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
    • D06M13/322Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing nitrogen
    • D06M13/325Amines
    • D06M13/342Amino-carboxylic acids; Betaines; Aminosulfonic acids; Sulfo-betaines
    • C11D2111/12
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M2101/00Chemical constitution of the fibres, threads, yarns, fabrics or fibrous goods made from such materials, to be treated
    • D06M2101/16Synthetic fibres, other than mineral fibres
    • D06M2101/30Synthetic polymers consisting of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M2101/32Polyesters

Abstract

The invention belongs to the technical field of textile printing and dyeing in textile industry printing and dyeing production, and particularly relates to a bio-based polyester degreasing agent, a preparation method and application thereof. The polyester degreasing agent is prepared from the following raw materials in parts by mass: 15-30% of tall oil modified surfactant, 2-15% of alkyl glycoside, 2-15% of cardanol polyoxyethylene ether, 2-15% of palm oil fatty acid sodium salt, 15-30% of natural oil sulfonated oil, 0.01-2% of tetrasodium glutamate diacetate, 0.01-2% of citric acid, 0.01-3% of magnesium chloride, 0.01-2% of defoaming agent and 20-50% of water. Meanwhile, the invention also discloses a corresponding preparation method. The polyester degreasing agent prepared by the invention has excellent acid and alkali resistance, good wetting, dispersing and emulsifying properties and strong decontamination and degreasing by utilizing the synergistic effect and the synergistic effect of the nonionic surfactant and the anionic surfactant. The polyester degreasing agent disclosed by the invention is natural and environment-friendly in raw material source, small in damage to textiles, free of harmful substances in wastewater after degreasing, and free of pollution to the environment.

Description

Bio-based polyester degreasing agent as well as preparation method and application thereof
Technical Field
The invention relates to the technical field of textile chemical industry, in particular to a bio-based polyester degreasing agent, and a preparation method and application thereof.
Background
The polyester is fiber-forming high polymer prepared by esterification or transesterification and polycondensation reaction of raw materials of Poly Terephthalic Acid (PTA) or dimethyl terephthalate (DMT) and ethylene glycol (MEG), and is prepared by spinning and post-treatment. Spinning oil is added into polyester during spinning and wiredrawing, and the oil can play roles of bundling, lubrication, friction coefficient reduction, static resistance and the like; other greasy dirt can be adhered to the fabric during the later weaving, dyeing and finishing processing, transportation and storage. Oligomers of 1-3% are also produced during the polyester spinning process. These greasy dirt and oligomers can affect the dyeing and finishing process of polyester fiber or fabric, and produce color bars, color spots, white powder and other defects.
The current common degreasing process is a complex chemical and physical chemical process carried out with alkali and terylene degreasing agents at a certain temperature, and comprises the actions of infiltration, cleaning, puffing, emulsification, saponification, dispersion, chelation and the like, so that the saponification and dissolution of grease are promoted, the grease is prevented from being re-adhered to fibers, and the degreasing effect is better under alkaline or neutral conditions, but the capability of removing oligomers is general.
The penetration and the cleaning are important functions of the degreasing agent, and the first step of the degreasing process is that the degreasing liquid penetrates into the fiber under the action of the surfactant to expand the fiber and impurities; the second step is a cleaning action, i.e. after the fiber is fully wetted, the impurities are removed by the actions of heat and soaping, emulsifying, dispersing, etc. of chemicals.
In order to improve the production efficiency and reduce the energy consumption, a degreasing and dyeing one-bath two-step process is adopted at present. The effective realization of the technology is necessary to rely on a composite multifunctional polyester degreasing agent which has the advantages of acid bath resistance, rapid permeation, strong emulsifying power, high detergency, high temperature resistance, oxidation resistance, hard water resistance, low foam, good dispersibility, good biodegradability, safety and no toxicity. It is not possible to combine the above properties with a single surfactant, and it is necessary to compound several surfactants to achieve satisfactory oil removal by synergistic and synergistic effects.
At present, various polyester degreasing agents commonly used for textiles contain substances such as APEO, phosphorus and the like, so that the printing and dyeing industry faces extremely high wastewater treatment pressure. Therefore, there is a continuous need in the art for a textile polyester degreasing agent which has an environment-friendly component, has a low influence on the environment, can easily treat the generated wastewater, and can maintain a good degreasing effect.
Disclosure of Invention
The invention aims to provide a bio-based polyester degreasing agent, a preparation method and application thereof, and aims to solve the problems, and the bio-based polyester degreasing agent is obtained by adopting specific raw materials for combination and matching with corresponding production processes, has excellent degreasing effect, and has consistent color depth, color light and brilliant brightness on the surface of dyed cloth, and no defects such as color bars, color spots, white powder, chicken feet marks and the like. The detergent has excellent acid and alkali resistance, good wetting, emulsifying, dispersing and defoaming performances and strong detergency. Part or all of the leveling agent and oligomer remover in the dyeing recipe can be replaced in a degreasing dyeing one-bath two-step process. The polyester degreasing agent disclosed by the invention is natural and environment-friendly in raw material source, small in damage to textiles, free of harmful substances in the generated process wastewater, free of pollution to the environment, capable of meeting the requirements of industry and good in application prospect. Meanwhile, the bio-based raw materials and the recycled raw materials are adopted, so that the energy consumption is greatly reduced, the pollution is reduced, the construction action path of the national 'double carbon' target is met, and the green low-carbon cyclic development in the industrial field is promoted.
The aim of the invention can be achieved by the following technical scheme:
the raw materials of the bio-based polyester degreasing agent comprise tall oil modified surfactant, alkyl glycoside, cardanol polyoxyethylene ether, palm oil fatty acid sodium salt, natural oil sulfonated oil, tetra sodium glutamate diacetate, citric acid, magnesium chloride, defoamer and water;
calculated by taking the total mass of the raw materials of the polyester degreasing agent as 100%, the polyester degreasing agent comprises the following components in percentage by mass:
Figure BSA0000293208780000021
Figure BSA0000293208780000031
wherein, the tall oil modified surfactant is prepared by reacting tall oil, ethylene oxide and propylene oxide;
the alkyl glycoside is any one or any combination of APG0810, APG1214 and APG 0814;
the cardanol polyoxyethylene ether is any one or any combination of a biotin-resistant organism NSS1305 and a biotin-resistant organism NSS A, NSS 1308;
the natural oil sulfonated oil is at least one or any combination of natural sulfonated rapeseed oil, natural sulfonated castor oil and sulfated natural beef tallow;
the defoamer is any one or any combination of polyoxypropylene polyoxyethylene glycerol ether and polyether modified polysiloxane.
A preparation method of a bio-based polyester degreasing agent comprises the following steps:
(1) Preparation of double metal cyanide catalysts: dissolving metal cyanide salt in water to obtain solution A, dissolving metal salt in water to obtain solution B, adding the solution B into the solution A under a high-speed stirring state, adding an organic complexing agent for reaction for a set time, and then obtaining the double metal cyanide catalyst by adopting a vacuum filtration or centrifugal separation method;
(2) Preparation of tall oil modified surfactant: adding tall oil and a double metal cyanide catalyst into a pressure-resistant reaction kettle, heating to 100-150 ℃ after oxygen removal, gradually adding a mixture of ethylene oxide and propylene oxide, carrying out polymerization reaction, curing for a set time after the reaction pressure is not changed any more, vacuumizing to remove residual monomers, obtaining the required tall oil modified surfactant, cooling and discharging for later use;
(3) Adding water into a reaction kettle, starting stirring, heating, adding citric acid and magnesium chloride, and stirring until the citric acid and the magnesium chloride are completely dissolved;
(4) Adding the tall oil modified surfactant, alkyl glycoside, cardanol polyoxyethylene ether, palm oil fatty acid sodium salt and natural oil sulfonated oil, and fully stirring and uniformly mixing;
(5) Cooling, adding tetrasodium glutamate diacetate and a defoaming agent, uniformly stirring, and filtering and discharging.
In the step (1), the organic complexing agent is any one or any combination of alcohol, ether and ester, preferably the combination of tertiary butanol and phthalate;
in step (1), the metal cyanide compound is K 3 [Fe(CN) 6 ]、Ag 3 [Co(CN) 6 ]、K 3 [Co(CN) 6 ]Any one or any combination of the above, preferably potassium hexacyanocobaltate K 3 [Co(CN) 6 ];
In the step (1), the metal salt is any one or any combination of ferric chloride, zinc chloride and zinc sulfate, preferably zinc chloride;
in the step (1), the molar ratio of the metal cyanide to the metal salt is 1:8-10;
in the step (1), the organic complexing agent needs to be added alternately and repeatedly, wherein the molar ratio of the using amount of the tertiary butanol to the total amount of the metal cyanide and the metal salt is (20-25) to 1, and the molar ratio of the phthalate to the total amount of the metal cyanide and the metal salt is (0.5-1) to 1;
in the step (1), the stirring rotation speed is 300rpm or more, preferably 8000rpm;
in the step (2), the mol ratio of the tall oil to the ethylene oxide to the propylene oxide is 1:5-15:3-5;
in the step (2), the double metal cyanide catalyst is used in the reaction in a mass ratio of 0.001-0.05%, preferably in a range of 0.004-0.01%; when the catalyst is lower than 0.001%, the reaction speed is slow, the heating and heat preserving time is prolonged, and the explosion aggregation is easy to occur; when the catalyst is more than 0.05%, the reaction speed is too high, the control is not good, and the explosion polymerization is easy to generate during the reaction;
in the step (2), the polymerization temperature is 100-150 ℃, preferably 130-150 ℃, and the polymerization pressure is 0.1-0.3MPa, preferably 0.2MPa;
in the step (4), the natural oil sulfonated oil is at least one or any combination of natural sulfonated rapeseed oil, natural sulfonated castor oil and sulfated natural beef tallow, preferably natural sulfonated rapeseed oil;
in the invention, the natural oil sulfonated oil is added in an amount of 15-30%, and the stability of the polyester degreasing agent is not obviously affected in the range.
In the step (5), the defoaming agent is any one or any combination of polyoxypropylene polyoxyethylene glycerol ether and polyether modified polysiloxane, preferably polyether modified polysiloxane, and can quickly permeate into the foam in a high-temperature foaming system to damage the stability of the foam, thereby achieving the defoaming effect.
In the step (1), the organic complexing agent is required to be added in batches for a plurality of times, and stirring, filtering and centrifugal separation are required after each addition, wherein the stirring time is 10 minutes each time, and the stirring speed is preferably 8000rpm;
in the step (1), after the last centrifugal separation, the obtained solid is required to be dried to constant weight under vacuum at 60 ℃;
in the step (2), the polymerization temperature is preferably 130-140 ℃;
in the step (3), the temperature is controlled to be 40-60 ℃;
in the step (4), the stirring time is more than 0.2 hours, preferably 0.5-1 hour;
in the step (5), the temperature is reduced to below 45 ℃.
The bio-based polyester degreasing agent is prepared by adopting the raw materials and the preparation method.
The application of the bio-based polyester degreasing agent is that the bio-based polyester degreasing agent or the bio-based polyester degreasing agent prepared by any method is used for finishing textiles.
The beneficial effects are that:
(1) The tall oil, also called liquid rosin, adopted by the invention is prepared from black solution remained in the process of preparing wood pulp by an alkaline method (mainly a sulfate method), and the processing and the utilization are important components of circular economy, and relate to sustainable recycling of forest resources, have a larger linkage relation to ecological environment and have larger economic benefit and social benefit. The modified low-carbon modified carbon fiber additive is prepared into a textile auxiliary raw material with proper performance, and the low-carbon and cyclic utilization of the textile raw material provides a powerful support for the green low-carbon sustainable development of the textile industry.
(2) The modified surfactant is obtained by embedding the ethylene oxide and the propylene oxide into tall oil. The ethylene oxide oil removal and emulsification effects are excellent; the epoxypropane has the effect of reducing foam while synergistically removing oil, and maintains the low-foam environment of the dye bath system.
(3) The alkyl glycoside adopted by the invention has low surface tension, no cloud point, adjustable HLB value, strong wetting power, strong detergency, rich and fine foam, strong compatibility, no toxicity, no harm, no stimulation to skin, rapid and thorough biodegradation, can be compounded with any type of surfactant, and has obvious synergistic effect. Has strong broad-spectrum antibacterial activity, easy dilution of the product, no gel phenomenon and convenient use. And the polyester degreasing agent has strong alkali resistance, strong acid resistance, hard water resistance and salt resistance, and is particularly suitable for preparing novel environment-friendly three-in-one high-efficiency polyester degreasing agent.
(4) The invention adopts natural oil sulfonated oil, which is an anionic sulfonated oil fatliquor prepared by taking natural oil as a main raw material, adopting a sulfur trioxide gas sulfonation process to modify and compounding with other necessary components, is an excellent anionic surfactant, and can prevent fabrics from causing rope wrinkles or being scratched to form color spots and hairiness. Excellent dispersion capability, improved oil removal capability, and improved oligomer 'powdery mildew', especially superfine fiber dyeing leveling and dispersion effects; and can reduce friction between fabrics and machines during dyeing, thereby preventing wrinkles, hairiness, bruise and "chicken feet".
(5) The tetrasodium glutamate diacetate adopted in the invention is a new generation of biodegradable green chelating agent, has stronger metal chelating capability, is prepared from renewable plant raw material L-glutamic acid, is safe and reliable to use, effectively replaces phosphorus chelating agent, and reduces wastewater treatment pressure.
(6) The cardanol polyoxyethylene ether, the palm oil fatty acid sodium salt and the citric acid adopted in the invention are all products which are natural in source, nontoxic and harmless, and quick and thorough in biodegradation, have no pollution to the environment, and reduce the sewage discharge of the dyeing pretreatment process; meanwhile, the product has mild effect, and the textile has small damage after being treated, can be widely applied to pretreatment short-flow processes such as cotton cloth, knots, knitting and the like, and is beneficial to the environment-friendly clean production of printing and dyeing enterprises.
(7) The invention provides a bio-based polyester degreasing agent, and a preparation method and application thereof, wherein the preparation method comprises the following steps: under the action of catalyst double metal cyanide, polymerizing tall oil, ethylene oxide and propylene oxide to obtain an initial product tall oil modified surfactant; and adding alkyl glycoside, cardanol polyoxyethylene ether, palm oil fatty acid sodium salt, natural oil sulfonated oil, tetra sodium glutamate diacetate, citric acid, magnesium chloride, a defoaming agent and water into the polymer to obtain the bio-based polyester degreasing agent. The polyester degreasing agent prepared by the invention has good application effect, the pH of the product is slightly acidic, meets the acid bath requirement of a novel one-bath two-step process for degreasing and dyeing polyester, and can replace part or all of leveling agents and oligomer removers in dyeing prescriptions; the fabric has the advantages of excellent acid and alkali resistance, good wetting, emulsifying, dispersing and defoaming performances, strong detergency, excellent oil removing effect, consistent color depth, consistent chromatic light and bright brightness of the dyed fabric surface, and no defects such as color bars, color spots, powdery mildew, chicken feet marks and the like.
(8) The bio-based product used in the invention has good biodegradability, is environment-friendly, can reduce the use amount of traditional petroleum-based chemicals, has low production cost and obvious economic benefit, is clean in production, and is beneficial to protecting ecological environment. Along with the enhancement of people's environmental awareness and the soundness of national environmental regulations, the textile printing and dyeing industry needs to develop towards biomass, and the green sustainable development of the industry is realized.
Detailed Description
For a better illustration of the present invention, which is convenient for understanding the technical solution of the present invention, exemplary but non-limiting examples of the present invention are as follows:
example 1
A bio-based polyester degreasing agent is prepared from the following raw materials in parts by mass: 16% of tall oil modified surfactant, 6% of APG 0815%, 4% of NSS1305A, 3% of NSS1308, 7% of palm oil fatty acid sodium salt, 20% of natural sulfonated rapeseed oil, 1% of tetrasodium glutamate diacetate, 0.5% of citric acid, 2% of magnesium chloride, 0.5% of defoamer and 41% of water;
the preparation method of the bio-based polyester degreasing agent in the embodiment comprises the following steps:
(1) Preparation of double metal cyanide catalysts: 8g of potassium hexacyanocobaltate was dissolved in 140ml of distilled water, 65g of a 38.5% by weight aqueous solution of zinc chloride was slowly added at 8000rpm, followed by addition of a mixture of 100ml of t-butanol and 100ml of distilled water, stirring for 20 minutes, and then, 14.7g of dimethyl phthalate and 200ml of distilled water were added, stirring for 10 minutes, and vacuum filtration was performed with a sand core funnel. 150ml of t-butanol and 60ml of distilled water were added to the obtained solid, stirred at 8000rpm for 10 minutes, 10.6g of dimethyl phthalate was added, stirring was continued for 10 minutes, and then centrifugal separation was performed. 200ml of t-butanol was added to the obtained solid, and the mixture was stirred at 8000rpm for 10 minutes, 6.7g of dimethyl phthalate was added, and the mixture was stirred for 10 minutes and then centrifuged. The solid was dried under vacuum at 60 ℃ to constant weight to give a solid powder catalyst.
(2) Preparation of tall oil modified surfactant: 340g of tall oil and 0.05g of double metal cyanide catalyst are added into a 2L reaction kettle, after the temperature is raised to 105 ℃ by vacuum pumping, 524g of mixture of Ethylene Oxide (EO) and 296g of Propylene Oxide (PO) are continuously added, the pressure of the reaction kettle is controlled to be about 0.2MPa, the reaction temperature is 130-135 ℃, after the monomer addition is finished, the pressure in the reaction kettle is not changed any more, the reaction kettle is cured for 30 minutes, then the vacuum pumping is carried out for 30 minutes, and the tall oil modified surfactant is obtained, and is discharged for standby.
(3) Adding water into a reaction kettle, starting stirring, heating to 40-60 ℃, adding citric acid and magnesium chloride, and stirring until the citric acid and the magnesium chloride are completely dissolved, wherein the stirring speed is 30-50rpm;
(4) Adding tall oil modified surfactant, alkyl glycoside, cardanol polyoxyethylene ether, palm oil fatty acid sodium salt and natural sulfonated rapeseed oil in a required proportion into a reaction kettle, and fully stirring and uniformly mixing;
(5) Cooling to below 45 ℃, adding tetrasodium glutamate diacetate and an antifoaming agent, uniformly stirring for 30 minutes, and filtering and discharging.
Example 2
The preparation conditions and the process in this example are basically the same as those in example 1, wherein the raw materials are as follows:
20% of tall oil modified surfactant, 5% of APG1214, 1305 4% of NSS1308, 8% of palm oil fatty acid sodium salt, 25% of natural sulfonated rapeseed oil, 1% of tetrasodium glutamate diacetate, 0.5% of citric acid, 2% of magnesium chloride, 0.5% of defoamer and 30% of water;
example 3
The preparation conditions and the process of the embodiment are basically the same as those of the embodiment 1, wherein the raw materials are as follows:
25% of tall oil modified surfactant, 1214 10% of APG, 2% of NSS1308, 10% of palm oil fatty acid sodium salt, 15% of natural sulfonated rapeseed oil, 1% of tetrasodium glutamate diacetate, 0.5% of citric acid, 2% of magnesium chloride, 0.5% of defoamer and 34% of water;
example 4
The preparation conditions and the process of the embodiment are basically the same as those of the embodiment 1, wherein the raw materials are as follows:
30% of tall oil modified surfactant, 1214 15% of APG, 2% of NSS1308, 3% of palm oil fatty acid sodium salt, 20% of natural sulfonated rapeseed oil, 1% of tetrasodium glutamate diacetate, 0.5% of citric acid, 2% of magnesium chloride, 0.5% of defoamer and 26% of water;
example 5
The preparation conditions and the process of the embodiment are basically the same as those of the embodiment 1, wherein the raw materials are as follows:
15% of tall oil modified surfactant, 0816 10% of APG, 6% of NSS1305A, 7% of NSS1308, 8% of palm oil fatty acid sodium salt, 25% of natural sulfonated rapeseed oil, 1% of tetrasodium glutamate diacetate, 0.5% of citric acid, 2% of magnesium chloride, 0.5% of defoamer and 25% of water;
comparative example 1
The degreasing agent Goon105A is a common degreasing agent in the market, and has good comprehensive effect.
The excellent polyester degreasing agent not only has good capability of reducing the surface tension of a solution and rapidly penetrating into the fiber, but also has excellent emulsifying, penetrating, dispersing, dissolving and cleaning capabilities for grease, wax, pigment, stains and the like. The existing polyester dyeing improvement process is a degreasing and dyeing one-bath two-step process, and the degreasing and dyeing processes are required to be completed under the acidic condition. The specific requirements on the polyester degreasing agent can be embodied by the following properties:
1. physical Property testing
Physical properties of bio-based polyester degreasing agents prepared in examples 1 to 5 of the present invention were tested, and the results are shown in table 1:
TABLE 1
Figure BSA0000293208780000091
As can be seen from Table 1, the bio-based polyester degreasing agent prepared by the invention has stable product, high content and good safety, is a polyester degreasing agent which can be used for textile processing and textile processing, has high safety and good application prospect.
2. Alkali resistance
100ml of solution containing 5g/L of scouring agent to be detected is prepared by adopting NaOH solutions with different concentrations, and the appearance state of the solution is observed: the solution did not delaminate and did not agglomerate or oil fly out, indicating that the scouring agent was resistant to alkali at this concentration, the higher the alkali concentration, the better the alkali resistance, and the test results are shown in table 2.
3. Permeability of
The penetration performance of the polyester degreasing agent is tested by the sedimentation time of a standard cotton canvas sheet according to the capability of the degreasing liquid on rapidly wetting fabrics at normal temperature.
1L of polyester degreasing agent solution to be detected with the concentration of 2g/L is prepared, the prepared standard cotton canvas sheet is immersed in the solution, and the canvas sedimentation time is recorded. The shorter the settling time, the better the permeability, and conversely the worse the test results are shown in table 2.
4. Emulsifying property
Good emulsifying effect, and can enable the fiber co-organisms and the external grease to be emulsified and removed from the fabric rapidly.
Adopting liquid paraffin to simulate grease, taking 20ml of liquid paraffin, 20ml of 25g/L polyester degreasing agent solution to be tested in a cylinder with a plug, preserving heat for 5 minutes at 34 ℃, oscillating for 10 times up and down, standing for 1 minute, repeating oscillating and standing operation for 5 times, standing for starting timing, recording the time from the layered liquid level to the scale of 10ml, wherein the longer the layered time is, the better the emulsifying property is, and the worse is the reverse, and the test result is shown in Table 2.
5. Foam Properties
The influence of the foam problem of the textile auxiliary on the production process cannot be ignored, firstly, the foam in the scouring liquid can cause white spots, spots or other flaws on the textile if not timely eliminated, secondly, the excessive foam can cause the reduction of the textile efficiency, and the too much foam can remain on the surface of textile equipment to erode the equipment, and finally, a large amount of foam overflows the textile system and can influence the surrounding environment and cause the waste of textile sizing agent. Therefore, the defoaming performance of the textile polyester degreasing agent is also very important.
100ml of the polyester degreasing agent solution to be tested with the concentration of 2g/L is prepared in a 250ml measuring cylinder, the oxygenation pump is used for foaming until the concentration of 250ml, oxygenation is stopped, the defoaming time when defoaming is carried out until the concentration of 120ml is measured by a stopwatch is recorded, the shorter the defoaming time is, the better the defoaming performance is, and the test result is shown in Table 2.
6. Dispersibility of
0.4g of disperse deep blue HGL 200%, 0.3g of terylene degreasing agent, 5g of buffer solution with pH of 4.5 and 94.3g of water are weighed to prepare 100ml of dye solution, and the dye solution is stirred for 10min; put one sheet in a Buchner funnel
Figure BSA0000293208780000101
The qualitative filter paper is pressed by a stainless steel ring, a vacuum pump is opened, and the pressure is opened to the maximum; 100ml of dye solution was poured into a Buchner funnel, the filtration time was recorded, and the residue of dye on the filter paper was observed. The higher the rating, the better the test results are shown in table 2.
Dispersibility at normal temperature: preparing 100ml of dye liquor at normal temperature, and filtering at normal temperature;
high temperature dispersibility: heating the prepared 100ml dye liquor to 130 ℃ in an infrared dyeing machine, preserving heat for 30 minutes, then cooling to 80 ℃, and taking out and filtering (a Buchner funnel must be soaked in water at 80 ℃);
residue rating criteria: 5 none, 4 a few, 3 a few, 2 more, 1 very heavy
7. Transfer dyeing property
Weighing 0.3g of polyester degreasing agent and 100g of water to prepare 100ml of polyester degreasing agent solution; the periphery of the color cloth and the white cloth with the same size are sewed, and the total weight of the cloth is 5g; placing the experimental cloth and 100ml of aqueous solution into a 200ml dyeing cup together to serve as a blank sample; placing the experimental cloth and 100ml of polyester degreasing agent solution into a 200ml dyeing cup to serve as a test sample; putting the dyeing cup into an infrared dyeing machine, heating to 130 ℃, preserving heat for 30 minutes, cooling to room temperature, taking out the test cloth, washing with water and drying. And observing the color change of the color-shifted cloth with the polyester degreasing agent and the blank color-shifted primary color cloth, and the color-shifted performance of the color-shifted cloth. The test is generally used to evaluate leveling performance, the higher the rating the better the test results are shown in Table 2.
Rating criteria: the intensity of the color-removed cloth of the polyester degreasing agent is 10% or more lower than that of the blank color-removed cloth, and no obvious color jump phenomenon exists;
3, the intensity of the polyester degreasing agent shifted color cloth and the intensity of the blank shifted color cloth are changed within 5%, and no obvious color jump phenomenon exists;
1, the intensity of the polyester degreasing agent color-shifted cloth is within 10 percent of that of the blank color-shifted cloth or has obvious color jump phenomenon;
TABLE 2
Figure BSA0000293208780000111
Figure BSA0000293208780000121
As can be seen from Table 2, the basic properties of the bio-based polyester degreasing agent prepared by the invention are better than or similar to those of comparative example 1.
8. Determination of oligomer content on fabrics by chloroform extraction
By using the similar principle of miscibility, the oligomer is dissolved by using an organic solvent. Chloroform is selected as the extractant because of its small molecular volume and ease of penetration into the fiber.
The one-bath two-step process of degreasing and dyeing is divided into two steps, wherein a degreasing agent and water are added into a dye vat for degreasing the polyester fabric, and working fluid is not discharged from the dye vat after the degreasing treatment; and in the second step, adding a dye and a dyeing auxiliary agent, and carrying out high Wen Diguan dyeing processing.
(1) Oil removal process prescription and process flow:
preparing a working solution with a bath ratio of 1:10 and a degreasing agent of 1g/l, pouring the working solution into a dyeing cup, adding polyester standard cloth, placing the dyeing cup into an infrared dyeing machine, heating to 80-85 ℃, preserving heat for 30min, and cooling to 35-45 ℃.
(2) Polyester high-temperature dyeing and post-treatment process prescription and process flow:
the dye liquor comprises the following components in percentage by mass:
Figure BSA0000293208780000122
the mass percentage of the reduction cleaning liquid is as follows:
Figure BSA0000293208780000123
Figure BSA0000293208780000131
adding water to complement the components, pouring the prepared dye liquor into a dyeing cup subjected to polyester degreasing treatment according to the mass percent of the dye liquor, placing the dyeing cup into an infrared dyeing machine, heating to 130-135 ℃, preserving heat for 40-50min, cooling to below 50 ℃, and discharging the dye liquor; then the cloth is treated for 10 to 20 minutes at the temperature of 75 to 85 ℃ by the reducing cleaning liquid and then discharged, and then the dyed cloth is sequentially washed by hot water, cold water, acid, cold water and dry,
taking 4g of dyed polyester fabric sample, and cutting into 25mm 2 The following chips were weighed out into an Erlenmeyer flask by weighing 3 parts of 1.0g (accurate to 0.01 g) of the sample from the chips. 50mL of chloroform was added separately, the conical flask was sealed with a film, placed in a 80℃water bath, kept under vigorous shaking for 2h, the sample was evaporated on a rotary evaporator after shaking (3 washes with chloroform, and the wash solution was poured into the evaporation flask), and when the volume of liquid in the evaporation flask was 5mL, it was dried under a nitrogen dryer, the evaporation flask was weighed on an electronic balance before placing the liquid, and the liquid was poured into the flask and the like, and was also weighed on the electronic balance after evaporation was completed. The difference between the two is the mass of the oligomer. The test results are shown in Table 3, with the lowest values indicating the lowest oligomer content.
TABLE 3 residual oligomer content on fabrics (mg)
Sample of Example 1 Example 2 Example 3 Example 4 Example 5 Comparative example 1
1# 13.2 13.3 14.9 13.4 12.6 30.5
2# 14.5 12.9 15.2 13.8 12.8 28.9
3# 14.1 12.7 14.2 14.2 13.1 31.2
9. Oil removal Performance test
A test method and evaluation of high-temperature degreasing and anti-rewet properties of a polyester fabric degreasing agent:
(1) A5 g white polyester fabric sample was prepared, the fabric was laid flat with 1ml syringe and each of the mixed oils (motor oil, 10# white oil, liquid paraffin=1:1:1), the syringe was separated from the fabric by about 4mm, and 0.05ml of oil was dropped onto the fabric by gently pushing the plunger. 2 drops are dropped to be shaped for 30 to 60 seconds at the temperature of 150 to 190 ℃ after the oil is moistened and opened, and then the dirty cloth is prepared for standby;
(2) Preparing 2g/l polyester degreasing agent working solution, putting a piece of dirty cloth and a piece of blank cloth sample into the working solution, placing the working solution into an infrared dyeing machine, heating to 100 ℃ at the speed of 2.0-4.0 ℃/min, preserving heat for 30min, cooling to 50-60 ℃ at the speed of 2.0-4.0 ℃/min, taking out the cloth, repeatedly cleaning the cloth with hot water at 80 ℃ for 4 times, and drying. The cleaning condition of the dirty cloth and the white cloth is observed, the dirty cloth is rated according to the dirty rating sample card of AATCC 130 soil release performance test, the higher the number of stages, the better the performance, and the test result is shown in Table 4.
TABLE 4 Table 4
Figure BSA0000293208780000141
As can be seen from tables 3 and 4, the bio-based polyester degreasing agent prepared by the invention has application performance superior to or similar to that of comparative example 1. The bio-based polyester prepared by the invention has stable and good degreasing, oligomer removal and leveling effects in the acid environment of a degreasing and dyeing one-bath two-step method by utilizing the synergistic effect and the synergistic effect of the anionic and nonionic surfactants; the source is natural and environment-friendly, the damage to the textile is small, and the generated process wastewater has no harmful substances and is environment-friendly.
It should be noted and appreciated that various modifications and improvements of the invention described in detail above can be made without departing from the spirit and scope of the invention as claimed in the appended claims. Accordingly, the scope of the claimed subject matter is not limited by any particular exemplary teachings presented.
The applicant states that the detailed method of the present invention is illustrated by the above examples, but the present invention is not limited to the detailed method described above, i.e. it does not mean that the present invention must be practiced in dependence upon the detailed method described above. It should be apparent to those skilled in the art that any modification of the present invention, equivalent substitution of raw materials for the product of the present invention, addition of auxiliary components, selection of specific modes, etc., falls within the scope of the present invention and the scope of disclosure.

Claims (10)

1. A bio-based polyester degreasing agent is characterized in that:
the polyester degreasing agent comprises the following raw materials of tall oil modified surfactant, alkyl glycoside, cardanol polyoxyethylene ether, palm oil fatty acid sodium salt, natural oil sulfonated oil, tetra sodium glutamate diacetate, citric acid, magnesium chloride, defoamer and water.
Calculated by taking the total mass of the raw materials of the polyester degreasing agent as 100%, the polyester degreasing agent comprises the following components in percentage by mass:
Figure FSA0000293208770000011
2. the bio-based polyester degreasing agent as claimed in claim 1, wherein:
the tall oil modified surfactant is prepared by reacting tall oil, ethylene oxide and propylene oxide;
the alkyl glycoside is any one or any combination of APG0810, APG1214 and APG 0816;
the cardanol polyoxyethylene ether is any one or any combination of a biotin-resistant organism NSS1305 and a biotin-resistant organism NSS A, NSS 1308;
the natural oil sulfonated oil is at least one or any combination of natural sulfonated rapeseed oil, natural sulfonated castor oil and sulfated natural beef tallow;
the defoamer is any one or any combination of polyoxypropylene polyoxyethylene glycerol ether and polyether modified polysiloxane.
3. The preparation method of the bio-based polyester degreasing agent is characterized by comprising the following steps of:
(1) Preparation of double metal cyanide catalysts: and dissolving the metal cyanide salt in water to obtain solution A, and dissolving the metal salt in water to obtain solution B. Adding the solution B into the solution A under a high-speed stirring state, adding a mixed organic complexing agent for reacting for a period of time, and then adopting a vacuum filtration or centrifugal separation method to obtain a solid catalyst;
(2) Preparation of tall oil modified surfactant: adding tall oil and a double metal cyanide catalyst into a pressure-resistant reaction kettle, heating to 100-150 ℃ after oxygen removal, gradually adding an EO/PO mixture, carrying out polymerization reaction, curing for a period of time after the reaction pressure is not changed any more, vacuumizing to remove residual monomers, obtaining the required tall oil modified surfactant, and discharging for later use;
(3) Adding water into a reaction kettle, starting stirring, heating, adding citric acid and magnesium chloride, and stirring until the citric acid and the magnesium chloride are completely dissolved;
(4) Adding the tall oil modified surfactant, alkyl glycoside, cardanol polyoxyethylene ether, palm oil fatty acid sodium salt and natural oil sulfonated oil, and fully stirring and uniformly mixing;
(5) Cooling, adding tetrasodium glutamate diacetate and a defoaming agent, uniformly stirring, and filtering and discharging.
4. The method for preparing the bio-based polyester degreasing agent according to claim 3, wherein the method comprises the following steps:
in the step (1), the adopted organic complexing agent is any one or any combination of alcohol, ether and ester;
in the step (1), the adopted organic complexing agent is a combination of tertiary butanol and phthalate.
5. The method for preparing the bio-based polyester degreasing agent according to claim 3, wherein the method comprises the following steps:
in the step (1), the metal cyanide compound is K 3 [Fe(CN) 6 ]、Ag 3 [Co(CN) 6 ]、K 3 [Co(CN) 6 ]Any one or any combination of the above;
the metal salt is any one or any combination of ferric chloride, zinc chloride and zinc sulfate.
6. The method for preparing the bio-based polyester degreasing agent according to claim 3, wherein the method comprises the following steps:
in the step (1), the stirring rotation speed is 300rpm.
7. The method for preparing the bio-based polyester degreasing agent according to claim 3, wherein the method comprises the following steps:
in the step (2), the polymerization temperature is 100-150 ℃ and the polymerization pressure is 0.1-0.3MPa.
8. A bio-based polyester degreasing agent is characterized in that: prepared by the preparation method according to any one of claims 3 to 7.
9. The application of the bio-based polyester degreasing agent is characterized in that: use of the polyester degreasing agent according to any one of claims 1 to 2 for finishing textiles.
10. The application of the bio-based polyester degreasing agent is characterized in that: the bio-based polyester degreasing agent prepared by the method of any one of claims 3 to 7 is used for finishing textiles.
CN202310015705.XA 2023-01-05 2023-01-05 Bio-based polyester degreasing agent as well as preparation method and application thereof Pending CN116376647A (en)

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