WO2022165929A1 - Preparation method for super-hydrophobic acrylic emulsion - Google Patents

Preparation method for super-hydrophobic acrylic emulsion Download PDF

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WO2022165929A1
WO2022165929A1 PCT/CN2021/081161 CN2021081161W WO2022165929A1 WO 2022165929 A1 WO2022165929 A1 WO 2022165929A1 CN 2021081161 W CN2021081161 W CN 2021081161W WO 2022165929 A1 WO2022165929 A1 WO 2022165929A1
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emulsion
super
acrylic emulsion
hydrophobic acrylic
emulsifier
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PCT/CN2021/081161
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French (fr)
Chinese (zh)
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周健彬
房迎春
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上海保立佳新材料有限公司
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F212/00Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
    • C08F212/02Monomers containing only one unsaturated aliphatic radical
    • C08F212/04Monomers containing only one unsaturated aliphatic radical containing one ring
    • C08F212/06Hydrocarbons
    • C08F212/08Styrene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/22Emulsion polymerisation
    • C08F2/24Emulsion polymerisation with the aid of emulsifying agents
    • C08F2/26Emulsion polymerisation with the aid of emulsifying agents anionic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/22Emulsion polymerisation
    • C08F2/24Emulsion polymerisation with the aid of emulsifying agents
    • C08F2/30Emulsion polymerisation with the aid of emulsifying agents non-ionic
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/38Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation

Definitions

  • the invention belongs to the technical field of emulsion preparation, in particular to a preparation method of a super-hydrophobic acrylic emulsion.
  • the preparation methods of acrylate emulsions include solution polymerization, precipitation polymerization, inverse emulsion polymerization and emulsion polymerization.
  • Emulsion polymerization uses water as the dispersion medium, does not pollute the environment, and can avoid the environmental pollution problems caused by the use of organic dispersion medium, such as high cost, poor storage stability, and solvent removal. It has become the main synthesis method of acrylate thickeners.
  • the existing emulsions have problems of poor hydrophobicity and poor stain resistance.
  • the purpose of the present invention is to solve the problem of poor anti-fouling effect of the existing emulsion due to poor hydrophobicity.
  • an emulsifier with a total monomer content of 3-5% and water are fully stirred and mixed for 15-30 minutes, and then acrylate monomers, special functional monomers, and molecular weight adjustment are added.
  • the pre-emulsion is obtained by stirring and emulsifying the emulsifier for 30-60 minutes to obtain a pre-emulsion; the emulsifier and water with a total monomer content of 3-5% are stirred evenly, and then 3% of the pre-emulsion is added, and 60% of the initiator solution is added dropwise at the same time, and the reaction is 7- After 15 minutes, the seed emulsion was prepared; the remaining pre-emulsion and initiator solution were continuously added dropwise into the seed emulsion, and then the temperature was kept warm and cooled to 60°C for elimination. After the post-elimination was completed, the reaction was continued for 1 hour, and the temperature was lowered to below 40°C. , filter and discharge the material to obtain the super-hydrophobic acrylic emulsion.
  • the emulsifier is an anionic emulsifier
  • the anionic emulsifier is sodium dodecyl sulfate, sodium dodecylbenzenesulfonate, ethoxylated alkyl sulfate sodium salt, and alkyl ether sulfate sodium salt , at least one of fatty alcohol ether sulfate sodium salt.
  • the anionic emulsifier accounts for 2-10% of the total amount of the anionic emulsifier, acrylate monomers, special functional monomers and molecular weight regulators.
  • the acrylate monomer is N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethacrylate monomer
  • silicon-containing functional monomers or special resin cross-linking monomers are examples.
  • the special functional monomer is isobornyl methacrylate, including multiple groups of double bond functional monomers and hydrophobic macromolecular silicon-containing double bond polymerizable monomers, and the special functional monomers account for anionic emulsifier, 10-25% of the total amount of acrylate monomers, special functional monomers and molecular weight regulators.
  • the molecular weight regulator is thiol and its derivatives or primary, secondary and tertiary thiols, thiol esters and thiol ethers with 5 to 14 carbon atoms, and the molecular weight regulator accounts for anionic emulsifier, acrylic acid 0.15-0.60% of the total amount of ester monomers, special functional monomers and molecular weight regulators.
  • the initiator is one of sodium persulfate, ammonium persulfate, and potassium persulfate, and the initiator accounts for 5% of the total amount of anionic emulsifier, acrylate monomer, special functional monomer and molecular weight regulator. 0.1 ⁇ 0.6%.
  • the emulsification reaction in the step S300 is to add the remaining pre-emulsion and the initiator solution dropwise to the prepared seed emulsion, the dropping time is 2-3 hours, and the dropping temperature is 80-90° C.
  • the remaining pre-emulsion is The resin cross-linking agent is added when the liquid and the initiator solution are added dropwise to one third, and the resin cross-linking agent is ethylene glycol dimethacrylate.
  • the post-elimination treatment in the step S400 is specifically cooling the solution after the emulsification reaction to 60° C., adding an oxidant and a reducing agent and keeping the temperature for 1 hour, the oxidizing agent is tert-butyl hydroperoxide, and the reducing agent is FF6M .
  • an emulsifier with a total monomer content of 3-5% and water are fully stirred and mixed for 15-30 minutes, and then acrylate monomers, special functional monomers, and molecular weight adjustment are added.
  • the pre-emulsion is obtained by stirring and emulsifying the emulsifier for 30-60 minutes to obtain a pre-emulsion; the emulsifier and water with a total monomer content of 3-5% are stirred evenly, and then 3% of the pre-emulsion is added, and 60% of the initiator solution is added dropwise at the same time, and the reaction is 7- After 15 minutes, the seed emulsion was prepared; the remaining pre-emulsion and initiator solution were continuously added dropwise into the seed emulsion, and then the temperature was kept warm and cooled to 60°C for elimination. After the post-elimination was completed, the reaction was continued for 1 hour, and the temperature was lowered to below 40°C.
  • Fig. 1 is the flow chart of a kind of preparation method of super-hydrophobic acrylic emulsion of the present invention.
  • the preparation method of a kind of super-hydrophobic acrylic emulsion of the present embodiment the emulsifier and water of the total monomer amount of 3-5% are fully stirred and mixed for 15-30 minutes, and the ratio of the emulsifier is in different formulas There are different requirements, especially for particle size control and subsequent application performance, because in this application, the particle size will be controlled between 100-130nm as much as possible. If the amount of emulsifier is less than 3%, the synthesis stability will be affected. If the proportion of emulsifier is higher than 5%, the application properties of the emulsion such as water resistance will be greatly affected, so this comparison needs to be strictly controlled.
  • acrylate monomers special functional monomers, molecular weight regulators, and stir and emulsify for 30-60 minutes to obtain a pre-emulsion.
  • the reaction time for the emulsifier needs to be precisely controlled. If the emulsification time is higher than the required time, it will affect the The encapsulation effect of the emulsifier on the monomer is generally manifested in that the size of the relative micelle will be smaller. If the emulsification time is not enough, it will easily lead to poor emulsification effect, thereby affecting the stability of the micelle.
  • the emulsifier is an anionic emulsifier
  • the anionic emulsifier is sodium dodecyl sulfate, sodium dodecylbenzenesulfonate, ethoxylated alkyl sulfate sodium salt, and alkyl ether sulfate sodium salt , at least one of fatty alcohol ether sulfate sodium salt.
  • the anionic emulsifier accounts for 5-10% of the total amount of the anionic emulsifier, acrylate monomers, special functional monomers and molecular weight regulators, because in this aspect, the emulsion uses more functional monomers, while the functional monomers It is relatively more difficult to emulsifier, and anionic emulsifier is an emulsifier with relatively high emulsification efficiency, so the amount of anionic emulsifier added is relatively large when selecting, and if it is lower than this ratio, it will easily lead to slag, but Anionic emulsifiers are also emulsifiers with relatively large effects such as water resistance, so in the process of use, they will try to control within this ratio.
  • the acrylate monomer is N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethyl-N-(2-aminoethyl)-2-aminoethacrylate monomer
  • silicon-containing functional monomers or special resin cross-linking monomers are examples.
  • the special functional monomer is isobornyl methacrylate.
  • This functional monomer has a high TG ratio and other comprehensive effects, which can improve the hardness, scrub resistance, medium resistance, high gloss and other excellent effects of the film.
  • the special functional monomers account for the total amount of anionic emulsifiers, acrylate monomers, special functional monomers and molecular weight regulators 10-25% of the amount (although the hardness of the functional monomer is high, it still needs a high density to improve the hardness and the contact angle effect of the surface after film formation, so as to achieve a good super-hydrophobic effect. If used If the amount of functional monomer is less than this amount, it is easy to cause insufficient hardness after film formation, which makes the coating easy to wear.
  • the molecular weight regulator is thiol and its derivatives or primary, secondary and tertiary thiols, thiol esters and thiol ethers with 5 to 14 carbon atoms, and the molecular weight regulator accounts for anionic emulsifier, acrylic acid 0.15-0.60% of the total amount of ester monomers, special functional monomers and molecular weight regulators.
  • Selecting molecular regulators can well control the molecular weight of the resin, ensure that the relative molecular weight of the obtained resin is relatively moderate, and ensure that the obtained resin is more Uniformity, if the proportion of use is small, the control of the resin is not obvious, and if the proportion of use is large, the molecular weight control is too low, and too low molecular weight will easily lead to insufficient strength and compactness of the coating, thus comprehensive performance will also be affected.
  • the initiator is one of sodium persulfate, ammonium persulfate, and potassium persulfate, and the initiator accounts for 5% of the total amount of anionic emulsifier, acrylate monomer, special functional monomer and molecular weight regulator. 0.1 ⁇ 0.6%.
  • the emulsification reaction in the step S300 is to add the remaining pre-emulsion and the initiator solution dropwise to the prepared seed emulsion, the dropping time is 2-3 hours, and the dropping temperature is 80-90° C.
  • the resin crosslinking agent is added when the liquid and initiator solution are added dropwise to one third. If the resin crosslinking agent used is added early, the latex particles are unstable during the initial reaction, and the degree of crosslinking is large, it is easy to slag. If the addition time is too late, it will not have a good cross-linking effect. According to the repeated test results in the laboratory, it is finally found that the overall improvement effect is more obvious in one third of the time.
  • the resin cross-linking agent is Ethylene glycol dimethacrylate.
  • the post-elimination treatment in step S400 is specifically to cool the solution after the emulsification reaction to 60° C., add an oxidant and a reducing agent and keep the temperature for 1 hour, the oxidant is tert-butyl hydroperoxide, and the reducing agent is FF6M.
  • emulsion To prepare the emulsion, weigh 160 g of deionized water, 10 g of emulsifier K12 and environmentally friendly non-ionic emulsifier, stir for 15 minutes, add 250.4 g of styrene, methyl methyl ester, 132.3 g of butyl acrylate and isooctyl acrylate, and 50 g of methyl acrylate. Isobornyl acrylate, 14.2 g of special functional monomers, and 0.5 g of dodecyl mercaptan were stirred for 30 minutes to obtain a pre-emulsion.
  • the temperature is lowered to below 40° C., and the material is filtered with a 200-mesh filter cloth to obtain a superhydrophobic acrylic emulsion with a solid content of 46-48%, a pH of 7-9, and a viscosity of less than 100 mPa.s.
  • the pH was adjusted with ammonia; the test added a certain amount of film-forming aid to the resin emulsion, and brushed it on the surface of the paint to test the dripping test.
  • the stain effect can meet the requirements of the national standard, and the water resistance of the tested emulsion is excellent.
  • acrylic resin is not excellent in water resistance, but it provides a good surface treatment of dripping water and beading, as well as excellent water resistance.

Abstract

A preparation method for a super-hydrophobic acrylic emulsion, comprising: fully stirring and mixing an emulsifier accounting for 3-5% of the total monomer amount and water for 15-30 minutes, then adding an acrylate monomer, a special functional monomer and a molecular weight regulator, and stirring and emulsifying same for 30-60 minutes to obtain a pre-emulsion; uniformly stirring an emulsifier accounting for 3-5% of the total monomer amount and water, adding 3% of the pre-emulsion, and dropwise adding 60% of an initiator solution at the same time for a reaction for 7-15 minutes to prepare a seed emulsion; and continuously dropwise adding the residual pre-emulsion and the initiator solution into the seed emulsion, then maintaining the temperature and then cooling same to 60ºC for post-elimination, continuously maintaining the temperature for a reaction for 1 hour after the completion of the post-elimination, cooling same to 40ºC or below, and then filtering and discharging same to obtain a super-hydrophobic acrylic emulsion. The preparation method has a simple process, the product is green and environmentally friendly, which effectively solves the problem of the water resistance of an existing acrylic resin being not good enough, and provides a good surface effect of dripping water into beads and a good water resistance effect.

Description

一种超疏水丙烯酸乳液的制备方法A kind of preparation method of super-hydrophobic acrylic emulsion 技术领域technical field
本发明属于乳液制备技术领域,具体来说是一种超疏水丙烯酸乳液的制备方法。The invention belongs to the technical field of emulsion preparation, in particular to a preparation method of a super-hydrophobic acrylic emulsion.
背景技术Background technique
目前在涂料行业,随着人们环保意识的增强和环保法规对有机挥发溶剂的限制,水分散体系或者水基涂料正在越来越多的领域取代以有机溶剂为分散相的传统涂料和油漆,水基涂料在储存和施工等阶段对体系的粘度有不同的要求,在很多应用场合需要一种特殊的超疏水罩面乳液,以达到很好的防水及耐污渍效果,不同于其他的超疏水乳液,该丙烯酸超疏水乳液更多的作为一款罩面乳液,保持原涂料的基础上,通过很简单是使用方式,达到很好的超疏水效果,在对此乳液进行测试,较高的乳液膜硬度,滴水成珠,减少水的残留,以及优异的耐沾污效果。At present, in the coatings industry, with the enhancement of people's awareness of environmental protection and the restriction of organic volatile solvents by environmental protection regulations, water dispersion systems or water-based coatings are replacing traditional coatings and paints with organic solvents as the dispersed phase in more and more fields. Base coatings have different requirements on the viscosity of the system during storage and construction. In many applications, a special superhydrophobic finish emulsion is required to achieve good waterproof and stain resistance, which is different from other superhydrophobic emulsions. , the acrylic super-hydrophobic emulsion is more used as an overcoat emulsion. On the basis of maintaining the original coating, it can achieve a very good super-hydrophobic effect through a very simple way of use. In the test of this emulsion, the higher the emulsion film Hardness, dripping into beads, reducing water residue, and excellent stain resistance.
目前,丙烯酸酯类乳液的制备方法有溶液聚合、沉淀聚合、反相乳液聚合和乳液聚合等。乳液聚合以水作为分散介质,不污染环境,可以避免利用有机分散介质所带来的成本高、储存稳定性差、溶剂脱除等环境污染问题,已成为丙烯酸酯类增稠剂的主要合成方法。但是现有的乳液存在疏水性差和耐沾污效果差的问题。At present, the preparation methods of acrylate emulsions include solution polymerization, precipitation polymerization, inverse emulsion polymerization and emulsion polymerization. Emulsion polymerization uses water as the dispersion medium, does not pollute the environment, and can avoid the environmental pollution problems caused by the use of organic dispersion medium, such as high cost, poor storage stability, and solvent removal. It has become the main synthesis method of acrylate thickeners. However, the existing emulsions have problems of poor hydrophobicity and poor stain resistance.
发明内容SUMMARY OF THE INVENTION
1.发明要解决的技术问题1. The technical problem to be solved by the invention
本发明的目的在于解决现有的乳液由于疏水性不佳导致的耐沾污效果差的问题。The purpose of the present invention is to solve the problem of poor anti-fouling effect of the existing emulsion due to poor hydrophobicity.
2.技术方案2. Technical solutions
为达到上述目的,本发明提供的技术方案为:For achieving the above object, the technical scheme provided by the invention is:
本发明的一种超疏水丙烯酸乳液的制备方法,将总单体量3~5%的乳化剂和水充分搅拌混合15-30分钟,后加入丙烯酸酯类单体、特殊功能单体、分子量调节剂搅拌乳化30-60分钟,得预乳化液;将总单体量3~5%的乳化剂和水搅拌均匀后加入3%的预乳化液,同时滴加60%引发剂溶液,反应7-15分钟后制得种子乳液;向种子乳液内继续滴加剩余预乳化液和引发剂溶液后保温并降温至60℃做后消除,后消除结束后继续保温反应1小时后,降温至40℃以下,过滤出料即得所述超疏水丙烯酸乳液。In the preparation method of the super-hydrophobic acrylic emulsion of the present invention, an emulsifier with a total monomer content of 3-5% and water are fully stirred and mixed for 15-30 minutes, and then acrylate monomers, special functional monomers, and molecular weight adjustment are added. The pre-emulsion is obtained by stirring and emulsifying the emulsifier for 30-60 minutes to obtain a pre-emulsion; the emulsifier and water with a total monomer content of 3-5% are stirred evenly, and then 3% of the pre-emulsion is added, and 60% of the initiator solution is added dropwise at the same time, and the reaction is 7- After 15 minutes, the seed emulsion was prepared; the remaining pre-emulsion and initiator solution were continuously added dropwise into the seed emulsion, and then the temperature was kept warm and cooled to 60°C for elimination. After the post-elimination was completed, the reaction was continued for 1 hour, and the temperature was lowered to below 40°C. , filter and discharge the material to obtain the super-hydrophobic acrylic emulsion.
优选的,所述乳化剂为阴离子乳化剂,所述阴离子乳化剂为十二烷基硫酸钠、十二烷基苯磺酸钠、乙氧基化烷基硫酸钠盐、烷基醚硫酸钠盐、脂肪醇醚硫酸酯钠盐中的至少一种。Preferably, the emulsifier is an anionic emulsifier, and the anionic emulsifier is sodium dodecyl sulfate, sodium dodecylbenzenesulfonate, ethoxylated alkyl sulfate sodium salt, and alkyl ether sulfate sodium salt , at least one of fatty alcohol ether sulfate sodium salt.
优选的,所述阴离子乳化剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的2~10%。Preferably, the anionic emulsifier accounts for 2-10% of the total amount of the anionic emulsifier, acrylate monomers, special functional monomers and molecular weight regulators.
优选的,所述丙烯酸酯类单体为Preferably, the acrylate monomer is
苯乙烯、甲甲酯、甲基丙烯酸和丙烯酸中的一种或多种;One or more of styrene, methyl methyl, methacrylic acid and acrylic acid;
or
丙烯酸丁酯、丙烯酸异辛酯、甲基丙烯酸甲酯中的一种或两种;One or both of butyl acrylate, isooctyl acrylate and methyl methacrylate;
或含硅类功能单体或特殊树脂交联型单体。Or silicon-containing functional monomers or special resin cross-linking monomers.
优选的,所述特殊功能单体为甲基丙烯酸异冰片酯,包括多组双键功能单体以及疏水大分子含硅类双键可聚合单体,所述特殊功能单体占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的10~25%。Preferably, the special functional monomer is isobornyl methacrylate, including multiple groups of double bond functional monomers and hydrophobic macromolecular silicon-containing double bond polymerizable monomers, and the special functional monomers account for anionic emulsifier, 10-25% of the total amount of acrylate monomers, special functional monomers and molecular weight regulators.
优选的,所述分子量调节剂为硫醇及其衍生物或5~14个碳原子的伯、仲、叔硫醇、硫醇酯和硫醇醚,所述分子量调节剂占阴离子乳化剂、丙烯酸酯类单 体、特殊功能单体和分子量调节剂总量的0.15~0.60%。Preferably, the molecular weight regulator is thiol and its derivatives or primary, secondary and tertiary thiols, thiol esters and thiol ethers with 5 to 14 carbon atoms, and the molecular weight regulator accounts for anionic emulsifier, acrylic acid 0.15-0.60% of the total amount of ester monomers, special functional monomers and molecular weight regulators.
优选的,所述引发剂为过硫酸钠、过硫酸铵、过硫酸钾中的一种,所述引发剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的0.1~0.6%。Preferably, the initiator is one of sodium persulfate, ammonium persulfate, and potassium persulfate, and the initiator accounts for 5% of the total amount of anionic emulsifier, acrylate monomer, special functional monomer and molecular weight regulator. 0.1~0.6%.
优选的,具体包括如下步骤:Preferably, it specifically includes the following steps:
S100、制备预乳化液;S100, preparing a pre-emulsion;
S200、制备种子乳液;S200, preparing seed emulsion;
S300、乳化反应;S300, emulsification reaction;
S400、后消除处理;S400, post-elimination processing;
S500、降温处理。S500, cooling treatment.
优选的,所述步骤S300中的乳化反应具体为向制备的种子乳液滴加剩余预乳化液和引发剂溶液,滴加时间2-3小时,滴加温度为80-90℃,当剩余预乳化液和引发剂溶液滴加三分之一时加入树脂交联剂,所述树脂交联剂为二甲基丙烯酸乙二醇酯。Preferably, the emulsification reaction in the step S300 is to add the remaining pre-emulsion and the initiator solution dropwise to the prepared seed emulsion, the dropping time is 2-3 hours, and the dropping temperature is 80-90° C. When the remaining pre-emulsion is The resin cross-linking agent is added when the liquid and the initiator solution are added dropwise to one third, and the resin cross-linking agent is ethylene glycol dimethacrylate.
优选的,所述步骤S400中的后消除处理具体为将乳化反应后的溶液降温至60℃,加入氧化剂和还原剂并保温1小时,所述氧化剂为叔丁基过氧化氢,还原剂为FF6M。Preferably, the post-elimination treatment in the step S400 is specifically cooling the solution after the emulsification reaction to 60° C., adding an oxidant and a reducing agent and keeping the temperature for 1 hour, the oxidizing agent is tert-butyl hydroperoxide, and the reducing agent is FF6M .
3.有益效果3. Beneficial effects
采用本发明提供的技术方案,与现有技术相比,具有如下有益效果:Adopting the technical scheme provided by the present invention, compared with the prior art, has the following beneficial effects:
本发明的一种超疏水丙烯酸乳液的制备方法,将总单体量3~5%的乳化剂和水充分搅拌混合15-30分钟,后加入丙烯酸酯类单体、特殊功能单体、分子量调节剂搅拌乳化30-60分钟,得预乳化液;将总单体量3~5%的乳化剂和水搅拌均匀后加入3%的预乳化液,同时滴加60%引发剂溶液,反应7-15分钟后制得种 子乳液;向种子乳液内继续滴加剩余预乳化液和引发剂溶液后保温并降温至60℃做后消除,后消除结束后继续保温反应1小时后,降温至40℃以下,过滤出料即得所述超疏水丙烯酸乳液。通过选用环保乳化剂、特殊功能单体、丙烯酸酯单体、分子量调节剂和后期树脂分子的交联剂通过乳液聚合得到,制备工艺简单,产品绿色环保,且很好的解决目前丙烯酸树脂耐水不够优异的效果,提供很好的滴水成珠的表面处理,以及优异的耐水效果。In the preparation method of the super-hydrophobic acrylic emulsion of the present invention, an emulsifier with a total monomer content of 3-5% and water are fully stirred and mixed for 15-30 minutes, and then acrylate monomers, special functional monomers, and molecular weight adjustment are added. The pre-emulsion is obtained by stirring and emulsifying the emulsifier for 30-60 minutes to obtain a pre-emulsion; the emulsifier and water with a total monomer content of 3-5% are stirred evenly, and then 3% of the pre-emulsion is added, and 60% of the initiator solution is added dropwise at the same time, and the reaction is 7- After 15 minutes, the seed emulsion was prepared; the remaining pre-emulsion and initiator solution were continuously added dropwise into the seed emulsion, and then the temperature was kept warm and cooled to 60°C for elimination. After the post-elimination was completed, the reaction was continued for 1 hour, and the temperature was lowered to below 40°C. , filter and discharge the material to obtain the super-hydrophobic acrylic emulsion. It is obtained through emulsion polymerization by selecting environmentally friendly emulsifiers, special functional monomers, acrylate monomers, molecular weight regulators and cross-linking agents for later resin molecules. Excellent effect, provides a very good dripping beading surface treatment, and excellent water resistance.
附图说明Description of drawings
图1为本发明的一种超疏水丙烯酸乳液的制备方法的流程图。Fig. 1 is the flow chart of a kind of preparation method of super-hydrophobic acrylic emulsion of the present invention.
具体实施方式Detailed ways
为了便于理解本发明,下面将参照相关附图对本发明进行更全面的描述,附图中给出了本发明的若干实施例,但是,本发明可以以许多不同的形式来实现,并不限于本文所描述的实施例,相反地,提供这些实施例的目的是使对本发明的公开内容更加透彻全面。In order to facilitate understanding of the present invention, the present invention will be more fully described below with reference to the related drawings, in which several embodiments of the present invention are given, however, the present invention may be implemented in many different forms and is not limited to this The described embodiments are, rather, provided so that this disclosure will be thorough and complete.
需要说明的是,当元件被称为“固设于”另一个元件,它可以直接在另一个元件上或者也可以存在居中的元件;当一个元件被认为是“连接”另一个元件,它可以是直接连接到另一个元件或者可能同时存在居中元件;本文所使用的术语“垂直的”、“水平的”、“左”、“右”以及类似的表述只是为了说明的目的。It should be noted that when an element is referred to as being "fixed" to another element, it can be directly on the other element or intervening elements may also be present; when an element is referred to as being "connected" to another element, it may be be directly connected to another element or intervening elements may be present; the terms "vertical", "horizontal", "left", "right" and similar expressions are used herein for illustrative purposes only.
除非另有定义,本文所使用的所有的技术和科学术语与属于本发明的技术领域的技术人员通常理解的含义相同;本文中在本发明的说明书中所使用的术语只是为了描述具体的实施例的目的,不是旨在于限制本发明;本文所使用的术语“及/或”包括一个或多个相关的所列项目的任意的和所有的组合。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the technical field of the present invention; the terms used herein in the description of the present invention are only used to describe specific embodiments is not intended to limit the invention; as used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
参照附图1,本实施例的一种超疏水丙烯酸乳液的制备方法,将总单体量3~5%的乳化剂和水充分搅拌混合15-30分钟,乳化剂的比例在不同的配方中具 有不同的要求,尤其在对于粒径的控制以及之后的应用性能,因为本申请中粒径会尽量控制在100-130nm之间,若乳化剂的量达不到3%,合成稳定性将受到很大的影响,若乳化剂的比例高于5%,乳液的应用性能比如耐水等等会受到很大的影响,所以对于此比较需要严格控制。后加入丙烯酸酯类单体、特殊功能单体、分子量调节剂搅拌乳化30-60分钟,得预乳化液,反应对于乳化剂的时间需要精确控制,乳化时间如果时间高于要求的时间,会影响乳化剂对于单体的包裹效果,总体表现在相对胶束的尺寸会跟细,若乳化的时间不够,则会容易导致乳化效果不好,从而在影响胶束的稳定性,;将总单体量3~5%的乳化剂和水搅拌均匀后加入3%的预乳化液,同时滴加60%引发剂溶液,反应7-15分钟后制得种子乳液;向种子乳液内继续滴加剩余预乳化液和引发剂溶液后保温并降温至60℃做后消除,后消除结束后继续保温反应1小时后,降温至40℃以下,过滤出料即得所述超疏水丙烯酸乳液。Referring to accompanying drawing 1, the preparation method of a kind of super-hydrophobic acrylic emulsion of the present embodiment, the emulsifier and water of the total monomer amount of 3-5% are fully stirred and mixed for 15-30 minutes, and the ratio of the emulsifier is in different formulas There are different requirements, especially for particle size control and subsequent application performance, because in this application, the particle size will be controlled between 100-130nm as much as possible. If the amount of emulsifier is less than 3%, the synthesis stability will be affected. If the proportion of emulsifier is higher than 5%, the application properties of the emulsion such as water resistance will be greatly affected, so this comparison needs to be strictly controlled. Then add acrylate monomers, special functional monomers, molecular weight regulators, and stir and emulsify for 30-60 minutes to obtain a pre-emulsion. The reaction time for the emulsifier needs to be precisely controlled. If the emulsification time is higher than the required time, it will affect the The encapsulation effect of the emulsifier on the monomer is generally manifested in that the size of the relative micelle will be smaller. If the emulsification time is not enough, it will easily lead to poor emulsification effect, thereby affecting the stability of the micelle. 3-5% of emulsifier and water are stirred evenly, and then 3% of pre-emulsion is added, and 60% of initiator solution is added dropwise at the same time, and the seed emulsion is obtained after 7-15 minutes of reaction; The emulsion and the initiator solution are then kept warm and cooled to 60°C for elimination. After the post-elimination, the reaction is continued for 1 hour, cooled to below 40°C, and filtered to obtain the super-hydrophobic acrylic emulsion.
具体的,所述乳化剂为阴离子乳化剂,所述阴离子乳化剂为十二烷基硫酸钠、十二烷基苯磺酸钠、乙氧基化烷基硫酸钠盐、烷基醚硫酸钠盐、脂肪醇醚硫酸酯钠盐中的至少一种。Specifically, the emulsifier is an anionic emulsifier, and the anionic emulsifier is sodium dodecyl sulfate, sodium dodecylbenzenesulfonate, ethoxylated alkyl sulfate sodium salt, and alkyl ether sulfate sodium salt , at least one of fatty alcohol ether sulfate sodium salt.
具体的,所述阴离子乳化剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的5~10%,因为此方面乳液使用的功能单体比较多,而功能单体相对更不容易乳化剂,而阴离子乳化剂属于乳化效率比较高的乳化剂,所以在选择的时候阴离子乳化剂的添加量相对较多,而若低于此比例,则容易导致出渣,但阴离子乳化剂也是属于耐水等效果影响比较大的乳化剂,所以在使用过程中,会尽量控制在此比例以内。Specifically, the anionic emulsifier accounts for 5-10% of the total amount of the anionic emulsifier, acrylate monomers, special functional monomers and molecular weight regulators, because in this aspect, the emulsion uses more functional monomers, while the functional monomers It is relatively more difficult to emulsifier, and anionic emulsifier is an emulsifier with relatively high emulsification efficiency, so the amount of anionic emulsifier added is relatively large when selecting, and if it is lower than this ratio, it will easily lead to slag, but Anionic emulsifiers are also emulsifiers with relatively large effects such as water resistance, so in the process of use, they will try to control within this ratio.
具体的,所述丙烯酸酯类单体为Specifically, the acrylate monomer is
苯乙烯、甲甲酯、甲基丙烯酸和丙烯酸中的一种或多种;One or more of styrene, methyl methyl, methacrylic acid and acrylic acid;
or
丙烯酸丁酯、丙烯酸异辛酯、甲基丙烯酸甲酯中的一种或两种;One or both of butyl acrylate, isooctyl acrylate and methyl methacrylate;
或含硅类功能单体或特殊树脂交联型单体。Or silicon-containing functional monomers or special resin cross-linking monomers.
具体的,所述特殊功能单体为甲基丙烯酸异冰片酯,此功能单体TG比较高且其他综合效果,可以很好的提高膜的硬度、耐擦洗、耐介质、高光泽等等优异效果,,包括多组双键功能单体以及疏水大分子含硅类双键可聚合单体,所述特殊功能单体占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的10~25%(虽然功能单体的硬度较高,但依然需要较高的致密度来提高硬度、成膜之后的表面的接触角效果,从而达到很好的超疏水效果。如果使用的功能单体的量少于此添加量,容易导致成膜之后的硬度不够,使涂层易磨损,若添加的比例较多,则交联太过于剧烈,导致乳液容易起渣)。Specifically, the special functional monomer is isobornyl methacrylate. This functional monomer has a high TG ratio and other comprehensive effects, which can improve the hardness, scrub resistance, medium resistance, high gloss and other excellent effects of the film. , including multiple groups of double bond functional monomers and hydrophobic macromolecular silicon-containing double bond polymerizable monomers, the special functional monomers account for the total amount of anionic emulsifiers, acrylate monomers, special functional monomers and molecular weight regulators 10-25% of the amount (although the hardness of the functional monomer is high, it still needs a high density to improve the hardness and the contact angle effect of the surface after film formation, so as to achieve a good super-hydrophobic effect. If used If the amount of functional monomer is less than this amount, it is easy to cause insufficient hardness after film formation, which makes the coating easy to wear.
具体的,所述分子量调节剂为硫醇及其衍生物或5~14个碳原子的伯、仲、叔硫醇、硫醇酯和硫醇醚,所述分子量调节剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的0.15~0.60%,选择分子调节剂可以很好的控制其树脂的分子量,保证所得的树脂相对分子量比较适中,确保所得是树脂的更加均一性,使用比例较少则对树脂的控制不明显,而使用比例较多,则分子量控制的太低,而过低的分子量会很容易导致其强度以及涂层的致密性不够,从而综合性能也会受到影响。Specifically, the molecular weight regulator is thiol and its derivatives or primary, secondary and tertiary thiols, thiol esters and thiol ethers with 5 to 14 carbon atoms, and the molecular weight regulator accounts for anionic emulsifier, acrylic acid 0.15-0.60% of the total amount of ester monomers, special functional monomers and molecular weight regulators. Selecting molecular regulators can well control the molecular weight of the resin, ensure that the relative molecular weight of the obtained resin is relatively moderate, and ensure that the obtained resin is more Uniformity, if the proportion of use is small, the control of the resin is not obvious, and if the proportion of use is large, the molecular weight control is too low, and too low molecular weight will easily lead to insufficient strength and compactness of the coating, thus comprehensive performance will also be affected.
具体的,所述引发剂为过硫酸钠、过硫酸铵、过硫酸钾中的一种,所述引发剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的0.1~0.6%。Specifically, the initiator is one of sodium persulfate, ammonium persulfate, and potassium persulfate, and the initiator accounts for 5% of the total amount of anionic emulsifier, acrylate monomer, special functional monomer and molecular weight regulator. 0.1~0.6%.
具体的,具体包括如下步骤:Specifically, it includes the following steps:
S100、制备预乳化液;S100, preparing a pre-emulsion;
S200、制备种子乳液;S200, preparing seed emulsion;
S300、乳化反应;S300, emulsification reaction;
S400、后消除处理;S400, post-elimination processing;
S500、降温处理。S500, cooling treatment.
具体的,所述步骤S300中的乳化反应具体为向制备的种子乳液滴加剩余预乳化液和引发剂溶液,滴加时间2-3小时,滴加温度为80-90℃,当剩余预乳化液和引发剂溶液滴加三分之一时加入树脂交联剂,所使用的树脂交联剂若添加时间较早,而初反应过程乳胶粒不稳定,交联程度较大则容易起渣,而添加的时间过晚,则其无法其很好的交联作用效果,根据实验室的反复测试效果,最后发现在三分之一的时候,总体提升效果更明显,所述树脂交联剂为二甲基丙烯酸乙二醇酯。Specifically, the emulsification reaction in the step S300 is to add the remaining pre-emulsion and the initiator solution dropwise to the prepared seed emulsion, the dropping time is 2-3 hours, and the dropping temperature is 80-90° C. When the remaining pre-emulsion is The resin crosslinking agent is added when the liquid and initiator solution are added dropwise to one third. If the resin crosslinking agent used is added early, the latex particles are unstable during the initial reaction, and the degree of crosslinking is large, it is easy to slag. If the addition time is too late, it will not have a good cross-linking effect. According to the repeated test results in the laboratory, it is finally found that the overall improvement effect is more obvious in one third of the time. The resin cross-linking agent is Ethylene glycol dimethacrylate.
具体的,步骤S400中的后消除处理具体为将乳化反应后的溶液降温至60℃,加入氧化剂和还原剂并保温1小时,所述氧化剂为叔丁基过氧化氢,还原剂为FF6M。Specifically, the post-elimination treatment in step S400 is specifically to cool the solution after the emulsification reaction to 60° C., add an oxidant and a reducing agent and keep the temperature for 1 hour, the oxidant is tert-butyl hydroperoxide, and the reducing agent is FF6M.
实施例1Example 1
制备乳化液,称取去离子水160g,乳化剂K12及环保型非离子乳化剂10g,搅拌15分钟,加入250.4g苯乙烯、甲甲酯,132.3g丙烯酸丁酯及丙烯酸异辛酯,50g甲基丙烯酸异冰片酯,14.2g特殊功能单体,0.5g十二烷基硫醇搅拌30分钟,即得预乳化液。To prepare the emulsion, weigh 160 g of deionized water, 10 g of emulsifier K12 and environmentally friendly non-ionic emulsifier, stir for 15 minutes, add 250.4 g of styrene, methyl methyl ester, 132.3 g of butyl acrylate and isooctyl acrylate, and 50 g of methyl acrylate. Isobornyl acrylate, 14.2 g of special functional monomers, and 0.5 g of dodecyl mercaptan were stirred for 30 minutes to obtain a pre-emulsion.
制备釜底物料,称取360g去离子水,8g乳化剂K12及非离子乳化剂搅拌10分钟。To prepare the bottom material of the kettle, weigh 360g of deionized water, 8g of emulsifier K12 and non-ionic emulsifier and stir for 10 minutes.
待釜内温度升至85℃时,加入5%的预乳液至釜内,加入5g过硫酸铵溶液(用5g水溶解0.25g过硫酸铵),反应10分钟得到种子乳液。When the temperature in the kettle rises to 85°C, add 5% pre-emulsion to the kettle, add 5g of ammonium persulfate solution (dissolve 0.25g of ammonium persulfate with 5g of water), and react for 10 minutes to obtain a seed emulsion.
滴加剩余乳化液和70g过硫酸铵溶液(用70g水溶解0.4g过硫酸铵),滴加时间2小时,滴加至乳化液的1/4时加入树脂多双键交联单体,反应温度控制在85-90℃。Add the remaining emulsion and 70g of ammonium persulfate solution (dissolve 0.4g of ammonium persulfate with 70g of water) dropwise for 2 hours, add resin multi-double bond cross-linking monomer when it is added dropwise to 1/4 of the emulsion, and react The temperature is controlled at 85-90°C.
滴加结束后,保温反应1小时。降温至60℃,加入叔丁基过氧化氢水溶液(5g水溶解0.18g叔丁基过氧化氢),间隔10分钟,加入FF6M水溶液(10g水溶解0.09g FF6M),加完保温1小时。After the dropwise addition was completed, the reaction was incubated for 1 hour. Cool down to 60 ℃, add tert-butyl hydroperoxide aqueous solution (5g water dissolves 0.18g tert-butyl hydroperoxide), interval 10 minutes, add FF6M aqueous solution (10g water dissolves 0.09g FF6M), add and keep warm for 1 hour.
保温结束后,降温至40℃以下,200目滤布过滤出料,即得超疏水丙烯酸乳液,固含为46-48%,pH为7-9,粘度小于100mPa.s。After the heat preservation is completed, the temperature is lowered to below 40° C., and the material is filtered with a 200-mesh filter cloth to obtain a superhydrophobic acrylic emulsion with a solid content of 46-48%, a pH of 7-9, and a viscosity of less than 100 mPa.s.
本示例制备的丙烯酸树脂,用氨水调节pH;测试将树脂乳液加入一定量成膜助剂,刷涂在涂料表面测试滴水实验,荷叶一样的滴水成珠效果,测试铅笔硬度在HB左右,耐沾污效果能满足国标要求,测试乳液耐水效果优异。For the acrylic resin prepared in this example, the pH was adjusted with ammonia; the test added a certain amount of film-forming aid to the resin emulsion, and brushed it on the surface of the paint to test the dripping test. The stain effect can meet the requirements of the national standard, and the water resistance of the tested emulsion is excellent.
通过选用环保乳化剂、特殊功能单体、丙烯酸酯单体、分子量调节剂和后期树脂分子的交联剂通过乳液聚合得到,制备工艺简单,产品绿色环保。通过本发明制备的丙烯酸树脂在和普通的单组分丙烯酸树脂的对比中,通过引入特殊功能单体、分子量调整和特殊工艺极大的改变树脂成膜后的表面张力及硬度,很好的解决目前丙烯酸树脂耐水不够优异的效果,提供很好的滴水成珠的表面处理,以及优异的耐水效果。It is obtained through emulsion polymerization by selecting environmentally friendly emulsifiers, special functional monomers, acrylate monomers, molecular weight regulators and cross-linking agents of late resin molecules, the preparation process is simple, and the product is green and environmentally friendly. Compared with the common one-component acrylic resin, the acrylic resin prepared by the present invention greatly changes the surface tension and hardness of the resin after film formation by introducing special functional monomers, molecular weight adjustment and special technology, which is a good solution to the problem. At present, acrylic resin is not excellent in water resistance, but it provides a good surface treatment of dripping water and beading, as well as excellent water resistance.
以上所述实施例仅表达了本发明的某种实施方式,其描述较为具体和详细,但并不能因此而理解为对本发明专利范围的限制;应当指出的是,对于本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进,这些都属于本发明的保护范围;因此,本发明专利的保护范围应以所附权利要求为准。The above-mentioned embodiment only expresses a certain embodiment of the present invention, and its description is more specific and detailed, but it should not be construed as a limitation on the scope of the patent of the present invention; it should be pointed out that for those of ordinary skill in the art Said that, on the premise of not departing from the concept of the present invention, several modifications and improvements can be made, which all belong to the protection scope of the present invention; therefore, the protection scope of the patent of the present invention should be subject to the appended claims.

Claims (10)

  1. 一种超疏水丙烯酸乳液的制备方法,其特征在于:将总单体量3~5%的乳化剂和水充分搅拌混合15-30分钟,后加入丙烯酸酯类单体、特殊功能单体、分子量调节剂搅拌乳化30-60分钟,得预乳化液;将总单体量3~5%的乳化剂和水搅拌均匀后加入3%的预乳化液,同时滴加60%引发剂溶液,反应7-15分钟后制得种子乳液;向种子乳液内继续滴加剩余预乳化液和引发剂溶液后保温并降温至60℃做后消除,后消除结束后继续保温反应1小时后,降温至40℃以下,过滤出料即得所述超疏水丙烯酸乳液。A preparation method of super-hydrophobic acrylic emulsion, which is characterized in that: 3-5% of the total monomer content of emulsifier and water are fully stirred and mixed for 15-30 minutes, and then acrylate monomers, special functional monomers, molecular weights are added. The regulator is stirred and emulsified for 30-60 minutes to obtain a pre-emulsion; the 3-5% emulsifier and water of the total monomer are stirred evenly, and then 3% of the pre-emulsion is added, and 60% of the initiator solution is added dropwise at the same time. Reaction 7 After 15 minutes, the seed emulsion was prepared; the remaining pre-emulsion and the initiator solution were added dropwise to the seed emulsion, and the temperature was kept at 60°C, and the temperature was lowered to 60°C. Hereinafter, the superhydrophobic acrylic emulsion is obtained by filtering and discharging the material.
  2. 根据权利要求1所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述乳化剂为阴离子乳化剂,所述阴离子乳化剂为十二烷基硫酸钠、十二烷基苯磺酸钠、乙氧基化烷基硫酸钠盐、烷基醚硫酸钠盐、脂肪醇醚硫酸酯钠盐中的至少一种。The method for preparing a super-hydrophobic acrylic emulsion according to claim 1, wherein the emulsifier is an anionic emulsifier, and the anionic emulsifier is sodium dodecyl sulfate, dodecylbenzenesulfonic acid At least one of sodium, ethoxylated alkyl sulfate sodium salt, alkyl ether sulfate sodium salt, and fatty alcohol ether sulfate sodium salt.
  3. 根据权利要求2所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述阴离子乳化剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的2~10%。The method for preparing a super-hydrophobic acrylic emulsion according to claim 2, wherein the anionic emulsifier accounts for 2-2% of the total amount of the anionic emulsifier, acrylate monomers, special functional monomers and molecular weight regulators. 10%.
  4. 根据权利要求1所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述丙烯酸酯类单体为The preparation method of a kind of super-hydrophobic acrylic emulsion according to claim 1, is characterized in that: described acrylate monomer is
    苯乙烯、甲甲酯、甲基丙烯酸和丙烯酸中的一种或多种;One or more of styrene, methyl methyl, methacrylic acid and acrylic acid;
    or
    丙烯酸丁酯、丙烯酸异辛酯、甲基丙烯酸甲酯中的一种或两种;One or both of butyl acrylate, isooctyl acrylate and methyl methacrylate;
    或含硅类功能单体或特殊树脂交联型单体。Or silicon-containing functional monomers or special resin cross-linking monomers.
  5. 根据权利要求1所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述特殊功能单体为甲基丙烯酸异冰片酯,包括多组双键功能单体以及疏水大分子含硅类双键可聚合单体,所述特殊功能单体占阴离子乳化剂、丙烯酸酯类 单体、特殊功能单体和分子量调节剂总量的10~25%。The method for preparing a super-hydrophobic acrylic emulsion according to claim 1, wherein the special functional monomer is isobornyl methacrylate, including multiple groups of double-bond functional monomers and hydrophobic macromolecules containing silicon Double bond polymerizable monomer, the special functional monomer accounts for 10-25% of the total amount of anionic emulsifier, acrylate monomer, special functional monomer and molecular weight regulator.
  6. 根据权利要求1所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述分子量调节剂为硫醇及其衍生物或5~14个碳原子的伯、仲、叔硫醇、硫醇酯和硫醇醚,所述分子量调节剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的0.15~0.60%。The preparation method of a kind of super-hydrophobic acrylic emulsion according to claim 1, it is characterized in that: described molecular weight regulator is mercaptan and its derivative or primary, secondary, tertiary mercaptan of 5~14 carbon atoms, sulfur For alcohol esters and thiol ethers, the molecular weight regulator accounts for 0.15-0.60% of the total amount of anionic emulsifiers, acrylate monomers, special functional monomers and molecular weight regulators.
  7. 根据权利要求1所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述引发剂为过硫酸钠、过硫酸铵、过硫酸钾中的一种,所述引发剂占阴离子乳化剂、丙烯酸酯类单体、特殊功能单体和分子量调节剂总量的0.1~0.6%。The preparation method of a kind of super-hydrophobic acrylic emulsion according to claim 1, is characterized in that: described initiator is a kind of in sodium persulfate, ammonium persulfate, potassium persulfate, and described initiator accounts for anionic emulsifier , 0.1-0.6% of the total amount of acrylate monomers, special functional monomers and molecular weight regulators.
  8. 根据权利要求1所述的一种超疏水丙烯酸乳液的制备方法,其特征在于,具体包括如下步骤:The preparation method of a kind of super-hydrophobic acrylic emulsion according to claim 1, is characterized in that, specifically comprises the steps:
    S100、制备预乳化液;S100, preparing a pre-emulsion;
    S200、制备种子乳液;S200, preparing seed emulsion;
    S300、乳化反应;S300, emulsification reaction;
    S400、后消除处理;S400, post-elimination processing;
    S500、降温处理。S500, cooling treatment.
  9. 根据权利要求8所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述步骤S300中的乳化反应具体为向制备的种子乳液滴加剩余预乳化液和引发剂溶液,滴加时间2-3小时,滴加温度为80-90℃,当剩余预乳化液和引发剂溶液滴加三分之一时加入树脂交联剂,所述树脂交联剂为二甲基丙烯酸乙二醇酯。The method for preparing a super-hydrophobic acrylic emulsion according to claim 8, wherein the emulsification reaction in the step S300 is dropwise adding the remaining pre-emulsion and the initiator solution to the prepared seed emulsion, and the dropping time 2-3 hours, the dropping temperature is 80-90°C, when the remaining pre-emulsion and initiator solution are added dropwise by one third, add a resin cross-linking agent, the resin cross-linking agent is ethylene glycol dimethacrylate ester.
  10. 根据权利要求8所述的一种超疏水丙烯酸乳液的制备方法,其特征在于:所述步骤S400中的后消除处理具体为将乳化反应后的溶液降温至60℃,加入氧化剂和还原剂并保温1小时,所述氧化剂为叔丁基过氧化氢,还原剂为FF6M。The method for preparing a super-hydrophobic acrylic emulsion according to claim 8, wherein the post-elimination treatment in the step S400 is specifically cooling the solution after the emulsification reaction to 60°C, adding an oxidizing agent and a reducing agent, and keeping the temperature For 1 hour, the oxidizing agent was tert-butyl hydroperoxide, and the reducing agent was FF6M.
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