CN101974143B - Organic silicon modified epoxy acrylate aqueous dispersion and preparation method thereof - Google Patents
Organic silicon modified epoxy acrylate aqueous dispersion and preparation method thereof Download PDFInfo
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Abstract
本发明公开了一种有机硅改性环氧丙烯酸酯水分散体及其制备方法。该方法是先用聚醚型环氧稀释剂与环氧树脂进行复配,再和丙烯酸单体反应得到低粘度环氧丙烯酸酯预聚物;然后用顺丁烯二酸酐对其进行接枝改性,在分子链上引入亲水基团;最后将小分子氨基硅油和有机碱复配制成中和剂,对体系进行中和,加水稀释分散,调节固含量和粘度,得到可紫外光固化的有机硅改性环氧丙烯酸酯水分散体。该有机硅改性环氧丙烯酸酯水分散体具有60%以上的高固含量和1,500~5,500mPa.s的低粘度。经紫外光固化后的涂膜具有4H~6H的高硬度,良好的柔韧性和优异的耐水性,吸水率低至5.0%以下,可应用于家具、建筑、家用电器、造纸印刷等领域。The invention discloses an organic silicon modified epoxy acrylate aqueous dispersion and a preparation method thereof. The method is to use polyether type epoxy diluent and epoxy resin to compound, and then react with acrylic acid monomer to obtain low viscosity epoxy acrylate prepolymer; then use maleic anhydride to graft it Introduce a hydrophilic group on the molecular chain; finally, compound a small molecule amino silicone oil and an organic base to make a neutralizer, neutralize the system, add water to dilute and disperse, adjust the solid content and viscosity, and obtain a UV-curable Aqueous dispersion of silicone modified epoxy acrylate. The silicone-modified epoxy acrylate aqueous dispersion has a high solid content of more than 60% and a low viscosity of 1,500-5,500 mPa.s. The coating film cured by ultraviolet light has a high hardness of 4H-6H, good flexibility and excellent water resistance, and the water absorption rate is as low as 5.0%. It can be used in furniture, construction, household appliances, paper printing and other fields.
Description
技术领域 technical field
本发明涉及一种有机硅改性环氧丙烯酸酯水分散体,特别是涉及一种高固含、低粘度的紫外光固化有机硅改性环氧丙烯酸酯水分散体及其制备方法。The invention relates to an aqueous dispersion of silicone-modified epoxy acrylate, in particular to a high-solid-content, low-viscosity UV-curable silicone-modified epoxy acrylate aqueous dispersion and a preparation method thereof.
背景技术 Background technique
紫外光(UV)固化技术因为其高效、环保和节约能源而广泛应用于油漆、涂料、油墨和粘合剂等多个领域。随着人们对环境的关注,限制和减少挥发性有机物(VOC)排放法规的制定和实施,紫外光固化涂料正逐渐代替传统的溶剂型涂料。紫外光固化涂料的一般配方包含光引发剂、活性单体及光敏预聚物,即环氧丙烯酸酯、聚氨酯丙烯酸酯、丙烯酸酯(聚醚或聚酯)和不饱和聚酯。其中环氧丙烯酸树脂原料来源广泛,价格便宜,且主链中含有稳定的C-C键、苯环和醚键,具有良好的耐化学药品性、拉伸模量、机械性能等,因此成为制备水性紫外光固化涂料的主要基体树脂。但是常规的环氧丙烯酸酯预聚物往往存在粘度过大、成膜硬而脆、柔韧性欠佳等缺点,因此使用时需要加入一定量的活性单体,而活性单体的挥发性又使其成为潜在的环境污染源。因此,在制备紫外光固化涂料的过程中,开始尝试用环保溶剂“水”来代替活性单体,从此出现了水性紫外光(UV)固化技术。该技术结合了传统的UV固化技术和水性涂料技术的优点,成为紫外光固化涂料发展的一个主要方向。但是,随着光敏树脂的亲水改性和环保溶剂的加入,涂膜的性能出现某些负面影响,如加入过多的环保溶剂将影响干燥和固化速度,亲水基团的存在导致耐水性较差等问题,限制了其在很多行业的应用。随着资源与环境压力的日益增加,需要不断改善环保型水性光固化环氧丙烯酸酯树脂的性能,以拓展其应用领域。Ultraviolet (UV) curing technology is widely used in many fields such as paints, coatings, inks and adhesives because of its high efficiency, environmental protection and energy saving. With people's concern about the environment, the formulation and implementation of regulations to limit and reduce volatile organic compound (VOC) emissions, UV-curable coatings are gradually replacing traditional solvent-based coatings. The general formulation of UV-curable coatings includes photoinitiators, reactive monomers and photosensitive prepolymers, namely epoxy acrylates, urethane acrylates, acrylates (polyether or polyester) and unsaturated polyesters. Among them, epoxy acrylic resin has a wide range of raw materials, low price, and the main chain contains stable C-C bonds, benzene rings and ether bonds, and has good chemical resistance, tensile modulus, mechanical properties, etc. The main matrix resin of photocurable coatings. However, conventional epoxy acrylate prepolymers often have shortcomings such as excessive viscosity, hard and brittle film formation, and poor flexibility. It becomes a potential source of environmental pollution. Therefore, in the process of preparing UV-curable coatings, attempts have been made to replace active monomers with environmentally friendly solvent "water", and water-based ultraviolet (UV) curing technology has emerged since then. This technology combines the advantages of traditional UV curing technology and water-based coating technology, and has become a main direction for the development of UV curing coatings. However, with the hydrophilic modification of photosensitive resin and the addition of environmentally friendly solvents, some negative effects will appear on the performance of the coating film. For example, adding too much environmentally friendly solvent will affect the drying and curing speed, and the existence of hydrophilic groups will lead to water resistance. Poor and other problems limit its application in many industries. With the increasing pressure on resources and the environment, it is necessary to continuously improve the performance of environmentally friendly water-based photocurable epoxy acrylate resins to expand their application fields.
发明内容 Contents of the invention
本发明目的在于克服现有技术存在的粘度大,脆性高,柔韧性不好以及耐水性差的缺点,提供一种高固含、低粘度,力学性能和耐水性能优良的紫外光固化环氧丙烯酸酯水分散体及其制备方法。The purpose of the present invention is to overcome the shortcomings of high viscosity, high brittleness, poor flexibility and poor water resistance in the prior art, and provide a UV-curable epoxy acrylate with high solid content, low viscosity, excellent mechanical properties and water resistance Aqueous dispersions and methods for their preparation.
本发明的目的通过如下技术方案实现:The purpose of the present invention is achieved through the following technical solutions:
一种有机硅改性环氧丙烯酸酯水分散体的制备方法,包括如下步骤:A preparation method of silicone-modified epoxy acrylate aqueous dispersion, comprises the steps:
(1)低粘度环氧丙烯酸酯预聚物的制备:在容器中加入环氧树脂、聚醚型环氧稀释剂和阻聚剂;搅拌升温至70~75℃,滴加丙烯酸和催化剂,0.5~1h滴加完毕;随后升温至80℃~90℃,反应3~5h,测定体系酸值低于5mgKOH/g停止反应,得到经聚醚型环氧稀释剂降粘改性的环氧丙烯酸酯预聚物;(1) Preparation of low-viscosity epoxy acrylate prepolymer: add epoxy resin, polyether type epoxy diluent and polymerization inhibitor into the container; stir and heat up to 70-75°C, add acrylic acid and catalyst dropwise, 0.5 The dropwise addition is completed in ~1h; then the temperature is raised to 80°C~90°C, and the reaction is carried out for 3~5h. When the acid value of the measurement system is lower than 5mgKOH/g, the reaction is stopped, and the epoxy acrylate modified by polyether epoxy diluent for viscosity reduction is obtained. prepolymer;
所述的环氧树脂为双酚A型环氧树脂E-51、E-54或E-44;所述的聚醚型环氧稀释剂为数均分子量550~650的聚乙二醇二缩水甘油醚、数均分子量550~750的聚丙二醇二缩水甘油醚和三羟甲基丙烷三缩水甘油醚中的一种或两种;环氧树脂与聚醚型环氧稀释剂中的环氧基与丙烯酸的羧基的摩尔比为1∶1;环氧树脂与聚醚型环氧稀释剂的环氧基摩尔比为2∶1~1∶2;阻聚剂用量为环氧树脂、聚醚型环氧稀释剂和丙烯酸总质量的0.2%~0.4%;催化剂用量为环氧树脂、环氧稀释剂和丙烯酸总质量的0.5%~0.8%;The epoxy resin is bisphenol A epoxy resin E-51, E-54 or E-44; the polyether epoxy diluent is polyethylene glycol diglycidol with a number average molecular weight of 550-650 Ether, one or both of polypropylene glycol diglycidyl ether and trimethylolpropane triglycidyl ether with a number average molecular weight of 550-750; The molar ratio of the carboxyl group of acrylic acid is 1:1; the epoxy molar ratio of the epoxy resin and the polyether type epoxy diluent is 2:1~1:2; 0.2% to 0.4% of the total mass of oxygen diluent and acrylic acid; the amount of catalyst is 0.5% to 0.8% of the total mass of epoxy resin, epoxy diluent and acrylic acid;
(2)顺丁烯二酸酐接枝环氧丙烯酸酯预聚物的制备:将步骤(1)反应体系降温至50~60℃,加入顺丁烯二酸酐、催化剂和阻聚剂,搅拌均匀;采用分段升温法,50~60℃反应0.5~1h,随后升温至70~80℃反应0.5~1h,反应达到理论酸值时停止,得到侧链带有羧基的顺酐接枝环氧丙烯酸酯预聚物;所述顺丁烯二酸酐的摩尔用量为步骤(1)所得的环氧丙烯酸酯预聚物中侧羟基摩尔含量的40%~60%;(2) Preparation of maleic anhydride grafted epoxy acrylate prepolymer: cooling the reaction system in step (1) to 50-60°C, adding maleic anhydride, catalyst and polymerization inhibitor, and stirring evenly; Using segmental heating method, react at 50-60°C for 0.5-1h, then raise the temperature to 70-80°C for 0.5-1h, stop when the reaction reaches the theoretical acid value, and obtain maleic anhydride grafted epoxy acrylate with carboxyl group in the side chain Prepolymer; the molar dosage of the maleic anhydride is 40% to 60% of the side hydroxyl molar content in the epoxy acrylate prepolymer obtained in step (1);
所述催化剂和阻聚剂用量分别为步骤(1)中环氧丙烯酸酯预聚物总质量的0.5%~0.8%和0.2%~0.4%;The amount of the catalyst and the polymerization inhibitor is respectively 0.5% to 0.8% and 0.2% to 0.4% of the total mass of the epoxy acrylate prepolymer in step (1);
(3)有机硅改性环氧丙烯酸酯水分散体的制备:将步骤(2)的反应体系降温至40~50℃,加入阻聚剂,持续搅拌;将有机碱与小分子氨基硅油复配制成中和剂,对步骤(2)制得的侧链带有羧基的顺酐接枝环氧丙烯酸酯预聚物进行中和,中和度为60%~100%;加入去离子水,在搅拌下稀释和乳化分散,得到固含量在60%~90%的有机硅改性环氧丙烯酸酯水分散体;(3) Preparation of silicone-modified epoxy acrylate aqueous dispersion: cool down the reaction system in step (2) to 40-50°C, add a polymerization inhibitor, and continue stirring; compound organic base and small molecule amino silicone oil into a neutralizing agent, the side chain prepared in step (2) has a carboxyl maleic anhydride grafted epoxy acrylate prepolymer for neutralization, and the degree of neutralization is 60% to 100%; add deionized water, and Dilute and emulsify and disperse under stirring to obtain an aqueous dispersion of silicone-modified epoxy acrylate with a solid content of 60% to 90%;
所述有机碱为二甲氨基乙醇或三乙胺;所述氨基硅油的数均分子量为100~400;有机碱用量为顺丁烯二酸酐摩尔用量的60%~100%;氨基硅油和阻聚剂用量分别为步骤(2)中顺酐接枝环氧丙烯酸酯预聚物总质量的1.0%~2.0%和0.1~0.4%;The organic base is dimethylaminoethanol or triethylamine; the number average molecular weight of the amino silicone oil is 100 to 400; the amount of the organic base is 60% to 100% of the molar amount of maleic anhydride; the amino silicone oil and polymerization inhibitor The agent dosage is respectively 1.0%~2.0% and 0.1~0.4% of the total mass of the maleic anhydride grafted epoxy acrylate prepolymer in the step (2);
所述步骤(1)~(3)的阻聚剂为对甲氧基苯酚、对苯二酚或2,6-二叔丁基对甲酚;所述步骤(1)和步骤(2)的催化剂为四乙基溴化铵或N,N-二甲基苄胺。The polymerization inhibitor of described step (1)~(3) is p-methoxyphenol, hydroquinone or 2,6-di-tert-butyl p-cresol; The step (1) and step (2) The catalyst is tetraethylammonium bromide or N,N-dimethylbenzylamine.
为进一步实现本发明目的,所述理论酸值定义为顺丁烯二酸酐分子开环酯化后保留一个羧基时的体系酸值。To further realize the purpose of the present invention, the theoretical acid value is defined as the system acid value when a maleic anhydride molecule retains a carboxyl group after ring-opening esterification.
所述去离子水的用量优选为使有机硅改性环氧丙烯酸酯水分散体的固含量控制到60%~80%。The amount of the deionized water is preferably such that the solid content of the silicone-modified epoxy acrylate aqueous dispersion is controlled to 60%-80%.
所述环氧树脂与环氧稀释剂的环氧基摩尔比优选为1∶1。The epoxy group molar ratio of the epoxy resin to the epoxy diluent is preferably 1:1.
一种有机硅改性环氧丙烯酸酯水分散体,由上述方法制备。A silicone-modified epoxy acrylate water dispersion is prepared by the above method.
所述有机硅改性环氧丙烯酸酯水分散体固含量高于60%,粘度为1,500~5,500mPa.s。The solid content of the silicone-modified epoxy acrylate aqueous dispersion is higher than 60%, and the viscosity is 1,500-5,500 mPa.s.
所述水分散体的固含量可定义为水分散体中非水部分的质量百分含量。The solid content of the aqueous dispersion can be defined as the mass percentage of the non-aqueous part in the aqueous dispersion.
本发明的制备方法是将聚醚型环氧稀释剂与环氧树脂复配降粘,再与丙烯酸单体进行环氧开环酯化反应,从而在预聚物分子中引入低模量聚醚链段,提高分子活动性,从而达到降粘和增韧改性目的;丙烯酸的酯化反应可在分子链中引入双键,赋予预聚物以光敏性;再利用顺丁烯二酸酐与环氧树脂开环后生成的侧羟基进行半酯化反应,将亲水性羧基引入分子链,同时增加了预聚物中的双键含量;然后用小分子氨基硅油与有机碱复配制得中和剂,对预聚物中的羧基进行中和,得到低粘度的紫外光固化有机硅改性环氧丙烯酸酯预聚物;中和反应后,滴加去离子水进一步调节固含量和粘度,并搅拌均匀,得到透明或半透明的高固含、低粘度紫外光固化有机硅改性环氧丙烯酸酯水分散体。The preparation method of the present invention is to compound polyether type epoxy diluent and epoxy resin to reduce viscosity, and then carry out epoxy ring-opening esterification reaction with acrylic acid monomer, thereby introducing low modulus polyether into the prepolymer molecule chain segments to improve molecular mobility, so as to achieve the purpose of viscosity reduction and toughening modification; the esterification reaction of acrylic acid can introduce double bonds in the molecular chain, endowing the prepolymer with photosensitivity; and then use maleic anhydride and ring The side hydroxyl group generated after the ring opening of the epoxy resin undergoes a half-esterification reaction, introducing the hydrophilic carboxyl group into the molecular chain, and at the same time increasing the double bond content in the prepolymer; agent to neutralize the carboxyl groups in the prepolymer to obtain a low-viscosity UV-curable silicone-modified epoxy acrylate prepolymer; after the neutralization reaction, add deionized water dropwise to further adjust the solid content and viscosity, and Stir evenly to obtain a transparent or translucent high-solid-content, low-viscosity UV-curable silicone-modified epoxy acrylate aqueous dispersion.
本发明采用聚醚型环氧稀释剂对双酚A型环氧丙烯酸酯预聚物及其水分散体进行降粘和增韧改性,可以同时获得较高的固含量和较低的施工粘度,并改善了固化膜的柔韧性。The present invention adopts polyether type epoxy diluent to carry out viscosity reduction and toughening modification on bisphenol A type epoxy acrylate prepolymer and its aqueous dispersion, and can obtain higher solid content and lower construction viscosity at the same time , and improved the flexibility of the cured film.
去离子水的稀释和乳化分散程度与顺酐接枝环氧丙烯酸酯预聚物的羧基含量、中和度和去离子水的用量有关,预聚物的羧基含量越高,中和度越大,与去离子水的相溶性越好,在较低固含量时水分散体就越透明。The degree of dilution and emulsification dispersion of deionized water is related to the carboxyl content of the maleic anhydride grafted epoxy acrylate prepolymer, the degree of neutralization and the amount of deionized water. The higher the carboxyl content of the prepolymer, the greater the degree of neutralization , the better the compatibility with deionized water, the more transparent the aqueous dispersion is at lower solid content.
水分散体的粘度和预烘时间与固含量有关,固含量越小,粘度越小,预烘时间就越长。The viscosity and pre-drying time of the aqueous dispersion are related to the solid content, the smaller the solid content, the lower the viscosity, and the longer the pre-drying time.
本发明所得有机硅改性环氧丙烯酸酯水分散体具有可紫外光固化特性,固化产物具有优良的力学性能和耐水性。The silicone-modified epoxy acrylate aqueous dispersion obtained in the present invention has the property of being curable by ultraviolet light, and the cured product has excellent mechanical properties and water resistance.
与现有技术相比,本发明具有如下优点:Compared with prior art, the present invention has following advantage:
(1)本发明针对常规环氧丙烯酸酯预聚物粘度大、成膜硬而脆且柔韧性不好等缺点,采用聚醚型环氧稀释剂对其进行降粘和增韧改性。加入适当比例的聚醚型环氧稀释剂后,环氧树脂复配体系的初始粘度、环氧丙烯酸酯预聚物的粘度及顺酐接枝并经中和后的预聚物体系粘度均有大幅下降,降粘率可高达90%~99%。经聚醚改性的UV固化膜的柔韧性可从弯曲直径10mm以上提高到1~2mm。(1) In view of the shortcomings of conventional epoxy acrylate prepolymers such as high viscosity, hard and brittle film formation and poor flexibility, the present invention adopts polyether type epoxy diluent to carry out viscosity reduction and toughening modification on it. After adding an appropriate proportion of polyether-type epoxy diluent, the initial viscosity of the epoxy resin compound system, the viscosity of the epoxy acrylate prepolymer and the viscosity of the prepolymer system grafted with maleic anhydride and neutralized all have a significant difference. The viscosity reduction rate can be as high as 90% to 99%. The flexibility of the polyether-modified UV curable film can be increased from a bending diameter of more than 10mm to 1-2mm.
(2)本发明针对降粘改性后的光敏树脂耐水性较差、力学性能不佳等缺陷,采用小分子氨基硅油与有机碱复配制成中和剂,对羧基改性的光敏预聚物进行中和改性,从而在树脂结构中引入有机硅链段,明显提高了树脂固化膜的耐水性,吸水率可降至5.0%以下。(2) The present invention aims at defects such as poor water resistance and poor mechanical properties of the photosensitive resin after viscosity-reducing modification, and adopts small-molecule amino silicone oil and organic base to compound as a neutralizer, and the carboxyl-modified photosensitive prepolymer The neutralization modification is carried out, so that the organic silicon chain segment is introduced into the resin structure, the water resistance of the cured resin film is obviously improved, and the water absorption rate can be reduced to below 5.0%.
(3)本发明的制备方法具有工艺简单方便、无污染、环境友好、涂膜质量高、应用前景广泛等优点,是新一代绿色环保高性能化工产品,可应用于绿色家具、建筑装修、家用电器、造纸印刷等领域以及环境友好型涂料、油墨和粘合剂行业。(3) The preparation method of the present invention has the advantages of simple and convenient process, no pollution, environmental friendliness, high coating film quality, and wide application prospects. Electrical appliances, paper printing and other fields as well as environmentally friendly coatings, inks and adhesives industries.
具体实施方法Specific implementation method
下面结合实施例对本发明作进一步的说明,但是实施例并不构成对本发明要求保护范围的限制。The present invention will be further described below in conjunction with the examples, but the examples are not intended to limit the protection scope of the present invention.
实施例1Example 1
(1)将46.26g环氧树脂E-51、77.86g数均分子量为550~750的聚丙二醇二缩水甘油醚和0.32g的阻聚剂对苯二酚,加入带有搅拌桨、温度计、恒压漏斗和冷凝管的四口反应烧瓶中;将35.26g丙烯酸装入恒压漏斗中。其中,环氧树脂E-51与聚丙二醇二缩水甘油醚中的环氧基团摩尔比为1∶1,丙烯酸的羧基与环氧树脂复配体系的环氧基摩尔比为1∶1。待体系升温至75℃时,加入1.28g的催化剂四乙基溴化铵,并开始滴加丙烯酸,0.5h滴加完毕。继续升温至85℃,反应至体系酸值<5mgKOH/g时结束,降温,得到降粘改性的环氧丙烯酸酯预聚物。阻聚剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚和丙烯酸总质量的0.2%;催化剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚和丙烯酸总质量的0.8%。(1) Add 46.26g of epoxy resin E-51, 77.86g of polypropylene glycol diglycidyl ether with a number average molecular weight of 550 to 750 and 0.32g of inhibitor hydroquinone, and add it with a stirring paddle, a thermometer, and a thermostat. In the four-necked reaction flask of pressure funnel and condenser; 35.26g acrylic acid is packed in constant pressure funnel. Among them, the molar ratio of epoxy resin E-51 and epoxy group in polypropylene glycol diglycidyl ether is 1:1, and the molar ratio of carboxyl group of acrylic acid and epoxy resin compound system is 1:1. When the temperature of the system was raised to 75°C, 1.28g of catalyst tetraethylammonium bromide was added, and acrylic acid was added dropwise, and the dropwise addition was completed within 0.5h. Continue to raise the temperature to 85° C., the reaction ends when the acid value of the system is less than 5 mgKOH/g, and the temperature is lowered to obtain a viscosity-reduced modified epoxy acrylate prepolymer. The amount of polymerization inhibitor is 0.2% of the total mass of epoxy resin E-51, polypropylene glycol diglycidyl ether and acrylic acid; the amount of catalyst is 0.8% of the total mass of epoxy resin E-51, polypropylene glycol diglycidyl ether and acrylic acid.
(2)待体系降温至60℃,加入23.67g顺酐(顺丁烯二酸酐)、1.46g催化剂四乙基溴化铵和0.36g阻聚剂对苯二酚,搅拌反应0.5h,然后升温至75℃,反应达理论酸值75.80mgKOH/g时降温,终止反应。其中,顺酐的摩尔用量为环氧丙烯酸酯预聚物的侧羟基摩尔含量的50%,催化剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.8%,阻聚剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.2%,理论酸值为顺酐与环氧丙烯酸酯预聚物发生半酯化后的体系酸值。(2) After the system cools down to 60°C, add 23.67g of maleic anhydride (maleic anhydride), 1.46g of catalyst tetraethylammonium bromide and 0.36g of polymerization inhibitor hydroquinone, stir for 0.5h, then heat up To 75°C, when the reaction reaches a theoretical acid value of 75.80mgKOH/g, lower the temperature and terminate the reaction. Wherein, the molar dosage of maleic anhydride is 50% of the side hydroxyl molar content of epoxy acrylate prepolymer, the catalyst dosage is 0.8% of the total mass of epoxy acrylate prepolymer and maleic anhydride, and the polymerization inhibitor dosage is epoxy acrylate 0.2% of the total mass of the ester prepolymer and maleic anhydride, the theoretical acid value is the acid value of the system after the maleic anhydride and the epoxy acrylate prepolymer are half-esterified.
(3)待体系降温至50℃,加入0.36g阻聚剂对苯二酚和15.00g有机碱中和剂二甲氨基乙醇,进行中和反应。搅拌30min后加入21.22g去离子水调节固含量和体系粘度,得到高固含、低粘度的紫外光固化环氧丙烯酸酯水分散体,外观为黄褐色透明粘液。其中,体系的中和度为70%,固含量为90%,阻聚剂用量为顺酐接枝环氧丙烯酸酯预聚物总质量的0.2%。(3) After the system cools down to 50°C, add 0.36g of polymerization inhibitor hydroquinone and 15.00g of organic base neutralizing agent dimethylaminoethanol to carry out neutralization reaction. After stirring for 30 minutes, 21.22 g of deionized water was added to adjust the solid content and system viscosity to obtain a high solid content, low viscosity UV-curable epoxy acrylate aqueous dispersion with a yellow-brown transparent viscous appearance. Wherein, the degree of neutralization of the system is 70%, the solid content is 90%, and the amount of the polymerization inhibitor is 0.2% of the total mass of the maleic anhydride grafted epoxy acrylate prepolymer.
(4)向步骤(3)所得的环氧丙烯酸酯水分散体中加入活性稀释剂三丙二醇二丙烯酸酯,光引发剂2-羟基-2-甲基-1-苯基-1-丙酮(光引发剂1173),搅拌均匀后涂膜,并于60℃烘箱中预烘20min,然后用2KW的紫外灯照射5s,得到环氧丙烯酸酯固化膜。其中,光引发剂用量为环氧丙烯酸酯水分散体和活性稀释剂总质量的4%,活性稀释剂与顺酐接枝环氧丙烯酸酯预聚物的质量比为2∶8。(4) add reactive diluent tripropylene glycol diacrylate in the epoxy acrylate aqueous dispersion of step (3) gained, photoinitiator 2-hydroxyl-2-methyl-1-phenyl-1-acetone (light Initiator 1173), stir evenly, apply film, and pre-bake in an oven at 60°C for 20 minutes, and then irradiate with a 2KW ultraviolet lamp for 5s to obtain an epoxy acrylate cured film. Wherein, the amount of the photoinitiator is 4% of the total mass of the epoxy acrylate water dispersion and the reactive diluent, and the mass ratio of the reactive diluent to the maleic anhydride grafted epoxy acrylate prepolymer is 2:8.
经检测,环氧稀释剂聚丙二醇二缩水甘油醚与环氧树脂E-51复配后体系从初始粘度6,220mPa·s降至114mPa·s,降粘率为98.17%;经过降粘改性的环氧丙烯酸酯预聚物的体系粘度从35,080mPa·s降至1,340mPa·s,降粘率为96.16%;再经顺丁烯二酸酐改性后的体系粘度为10,840mPa·s,而不经降粘改性的对应预聚物体系粘度高达100,000mPa·s以上。加水稀释至90%固含量时,水分散体的粘度降至6,410mPa.s,表明环氧稀释剂的加入大大降低了体系粘度。UV固化后涂膜的铅笔硬度为4H,附着力为2级,冲击性能为30Kg·cm,弯曲性能为2mm,表明固化膜有较高的硬度和良好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为11.30%。After testing, the compounding of epoxy diluent polypropylene glycol diglycidyl ether and epoxy resin E-51 reduced the initial viscosity from 6,220mPa·s to 114mPa·s, and the viscosity reduction rate was 98.17%. The system viscosity of epoxy acrylate prepolymer dropped from 35,080mPa·s to 1,340mPa·s, and the viscosity reduction rate was 96.16%; The viscosity of the corresponding prepolymer system modified by viscosity reduction is as high as 100,000mPa·s or more. When diluted with water to 90% solid content, the viscosity of the aqueous dispersion dropped to 6,410mPa.s, indicating that the addition of epoxy diluent greatly reduced the viscosity of the system. After UV curing, the pencil hardness of the coating film is 4H, the adhesion is grade 2, the impact performance is 30Kg·cm, and the bending performance is 2mm, indicating that the cured film has high hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 11.30%.
实施例2Example 2
(1)将46.26g环氧树脂E-51、77.86g数均分子量为550~750的聚丙二醇二缩水甘油醚和0.48g的阻聚剂对甲氧基苯酚,加入带有搅拌桨、温度计、恒压漏斗和冷凝管的四口反应烧瓶中;将35.26g丙烯酸装入恒压漏斗中。其中,环氧树脂E-51与聚丙二醇二缩水甘油醚中的环氧基团摩尔比为1∶1,丙烯酸的羧基与环氧树脂复配体系的环氧基摩尔比为1∶1。待体系升温至75℃时,加入0.80g的催化剂N,N-二甲基苄胺,并开始滴加丙烯酸,0.5h滴加完毕。继续升温至85℃,反应至体系酸值<5mgKOH/g时结束,降温,得到降粘改性的环氧丙烯酸酯预聚物。阻聚剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚和丙烯酸总质量的0.3%;催化剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚和丙烯酸总质量的0.5%。(1) 46.26g of epoxy resin E-51, 77.86g of polypropylene glycol diglycidyl ether with a number average molecular weight of 550 to 750 and 0.48g of inhibitor p-methoxyphenol were added with stirring paddle, thermometer, In a four-necked reaction flask with a constant pressure funnel and a condenser; 35.26 g of acrylic acid was charged into the constant pressure funnel. Among them, the molar ratio of epoxy resin E-51 and epoxy group in polypropylene glycol diglycidyl ether is 1:1, and the molar ratio of carboxyl group of acrylic acid and epoxy resin compound system is 1:1. When the temperature of the system was raised to 75° C., 0.80 g of catalyst N,N-dimethylbenzylamine was added, and acrylic acid was added dropwise, and the dropwise addition was completed within 0.5 h. Continue to raise the temperature to 85° C., the reaction ends when the acid value of the system is less than 5 mgKOH/g, and the temperature is lowered to obtain a viscosity-reduced modified epoxy acrylate prepolymer. The amount of polymerization inhibitor is 0.3% of the total mass of epoxy resin E-51, polypropylene glycol diglycidyl ether and acrylic acid; the amount of catalyst is 0.5% of the total mass of epoxy resin E-51, polypropylene glycol diglycidyl ether and acrylic acid.
(2)待体系降温至60℃,加入23.67g顺酐、0.91g催化剂N,N-二甲基苄胺和0.54g阻聚剂对甲氧基苯酚,搅拌反应0.5h,然后升温至75℃,反应达理论酸值75.80mgKOH/g时降温,终止反应。其中,顺酐的摩尔用量为环氧丙烯酸酯预聚物的侧羟基摩尔含量的50%,催化剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.5%,阻聚剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.3%,理论酸值为顺酐与环氧丙烯酸酯预聚物发生半酯化后的体系酸值。(2) After the system cools down to 60°C, add 23.67g maleic anhydride, 0.91g catalyst N,N-dimethylbenzylamine and 0.54g polymerization inhibitor p-methoxyphenol, stir for 0.5h, then heat up to 75°C When the reaction reaches a theoretical acid value of 75.80 mgKOH/g, the temperature is lowered to terminate the reaction. Wherein, the molar dosage of maleic anhydride is 50% of the side hydroxyl molar content of epoxy acrylate prepolymer, the catalyst dosage is 0.5% of the total mass of epoxy acrylate prepolymer and maleic anhydride, and the polymerization inhibitor dosage is epoxy acrylate 0.3% of the total mass of ester prepolymer and maleic anhydride, the theoretical acid value is the acid value of the system after maleic anhydride and epoxy acrylate prepolymer undergo half-esterification.
(3)待体系降温至50℃,加入0.36g阻聚剂对甲氧基苯酚和15.00g有机碱中和剂二甲氨基乙醇,进行中和反应。搅拌30min后加入21.22g去离子水调节固含量和体系粘度,得到高固含、低粘度的紫外光固化环氧丙烯酸酯水分散体,外观为浅黄色透明粘液。其中,体系的中和度为70%,固含量为90%,阻聚剂用量为顺酐接枝环氧丙烯酸酯预聚物总质量的0.2%。(3) After the system cools down to 50°C, add 0.36g of polymerization inhibitor p-methoxyphenol and 15.00g of organic base neutralizing agent dimethylaminoethanol to carry out neutralization reaction. After stirring for 30 minutes, 21.22 g of deionized water was added to adjust the solid content and system viscosity to obtain a high solid content, low viscosity UV-curable epoxy acrylate aqueous dispersion, which appeared as light yellow transparent mucus. Wherein, the degree of neutralization of the system is 70%, the solid content is 90%, and the amount of the polymerization inhibitor is 0.2% of the total mass of the maleic anhydride grafted epoxy acrylate prepolymer.
(4)向步骤(3)所得的环氧丙烯酸酯水分散体中加入活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯,光引发剂2-羟基-2-甲基-1-苯基-1-丙酮(光引发剂1173),搅拌均匀后涂膜,并于60℃烘箱中预烘30min,然后用2KW的紫外灯照射5s,得到环氧丙烯酸酯固化膜。其中,光引发剂用量为环氧丙烯酸酯水分散体和活性稀释剂总质量的4%,活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯与顺酐接枝环氧丙烯酸酯预聚物的质量比为1∶1∶8。(4) Add reactive diluent tripropylene glycol diacrylate and trimethylolpropane triacrylate in the epoxy acrylate aqueous dispersion of step (3) gained, photoinitiator 2-hydroxyl-2-methyl-1 -Phenyl-1-acetone (photoinitiator 1173), stir evenly, apply film, and pre-bake in an oven at 60°C for 30min, and then irradiate with 2KW UV lamp for 5s to obtain a cured epoxy acrylate film. Wherein, the amount of photoinitiator is 4% of the total mass of epoxy acrylate aqueous dispersion and reactive diluent, reactive diluent tripropylene glycol diacrylate and trimethylolpropane triacrylate and maleic anhydride grafted epoxy acrylate The mass ratio of the prepolymer is 1:1:8.
与实施例1相比,本例中光敏预聚物的固化速度加快,交联度增加,UV固化后涂膜的铅笔硬度为5H,附着力为2级,冲击性能为35Kg·cm,弯曲性能为3mm,表明固化膜有更高的硬度和良好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为9.15%。Compared with Example 1, the curing speed of the photosensitive prepolymer in this example is accelerated, and the degree of crosslinking is increased. After UV curing, the pencil hardness of the coating film is 5H, the adhesion is grade 2, the impact performance is 35Kg cm, and the bending performance It is 3mm, indicating that the cured film has higher hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 9.15%.
实施例3Example 3
(1)将46.26g环氧树脂E-51、72.47g数均分子量为550~650的聚乙二醇二缩水甘油醚和0.31g的阻聚剂对甲氧基苯酚,加入带有搅拌桨、温度计、恒压漏斗和冷凝管的四口反应烧瓶中;将35.26g丙烯酸装入恒压漏斗中。其中,环氧树脂E-51与聚丙二醇二缩水甘油醚中的环氧基团摩尔比为1∶1,丙烯酸的羧基与环氧树脂复配体系的环氧基摩尔比为1∶1。待体系升温至75℃时,加入1.23g的催化剂N,N-二甲基苄胺,并开始滴加丙烯酸,0.5h滴加完毕。继续升温至85℃,反应至体系酸值<5mgKOH/g时结束,降温,得到降粘改性的环氧丙烯酸酯预聚物。阻聚剂用量为环氧树脂E-51、聚乙二醇二缩水甘油醚和丙烯酸总质量的0.2%;催化剂用量为环氧树脂E-51、聚乙二醇二缩水甘油醚和丙烯酸总质量的0.8%。(1) 46.26g of epoxy resin E-51, 72.47g of polyethylene glycol diglycidyl ether with a number average molecular weight of 550 to 650 and 0.31g of inhibitor p-methoxyphenol were added with stirring paddle, In the four-necked reaction flask of thermometer, constant pressure funnel and condenser; 35.26g acrylic acid is charged in constant pressure funnel. Among them, the molar ratio of epoxy resin E-51 and epoxy group in polypropylene glycol diglycidyl ether is 1:1, and the molar ratio of carboxyl group of acrylic acid and epoxy resin compound system is 1:1. When the temperature of the system was raised to 75°C, 1.23g of catalyst N,N-dimethylbenzylamine was added, and acrylic acid was added dropwise, and the dropwise addition was completed within 0.5h. Continue to raise the temperature to 85° C., the reaction ends when the acid value of the system is less than 5 mgKOH/g, and the temperature is lowered to obtain a viscosity-reduced modified epoxy acrylate prepolymer. The amount of polymerization inhibitor is 0.2% of the total mass of epoxy resin E-51, polyethylene glycol diglycidyl ether and acrylic acid; the amount of catalyst is the total mass of epoxy resin E-51, polyethylene glycol diglycidyl ether and acrylic acid 0.8%.
(2)待体系降温至60℃,加入23.67g顺酐、1.42g催化剂N,N-二甲基苄胺和0.36g阻聚剂对甲氧基苯酚,搅拌反应0.5h,然后升温至75℃,反应达理论酸值77.25mgKOH/g时降温,终止反应。其中,顺酐的摩尔用量为环氧丙烯酸酯预聚物的侧羟基摩尔含量的50%,催化剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.8%,阻聚剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.2%,理论酸值为顺酐与环氧丙烯酸酯预聚物发生半酯化后的体系酸值。(2) After the system cools down to 60°C, add 23.67g maleic anhydride, 1.42g catalyst N,N-dimethylbenzylamine and 0.36g polymerization inhibitor p-methoxyphenol, stir for 0.5h, then heat up to 75°C When the reaction reaches a theoretical acid value of 77.25mgKOH/g, the temperature is lowered to terminate the reaction. Wherein, the molar dosage of maleic anhydride is 50% of the side hydroxyl molar content of epoxy acrylate prepolymer, the catalyst dosage is 0.8% of the total mass of epoxy acrylate prepolymer and maleic anhydride, and the polymerization inhibitor dosage is epoxy acrylate 0.2% of the total mass of the ester prepolymer and maleic anhydride, the theoretical acid value is the acid value of the system after the maleic anhydride and the epoxy acrylate prepolymer are half-esterified.
(3)待体系降温至50℃,加入0.36g阻聚剂对甲氧基苯酚和15.00g有机碱中和剂二甲氨基乙醇,进行中和反应。搅拌30min后加入42.08g去离子水调节固含量和体系粘度,得到高固含、低粘度的紫外光固化环氧丙烯酸酯水分散体,外观为浅黄色透明粘液。其中,体系的中和度为70%,固含量为80%,阻聚剂用量为顺酐接枝环氧丙烯酸酯预聚物总质量的0.2%。(3) After the system cools down to 50°C, add 0.36g of polymerization inhibitor p-methoxyphenol and 15.00g of organic base neutralizing agent dimethylaminoethanol to carry out neutralization reaction. After stirring for 30 minutes, 42.08 g of deionized water was added to adjust the solid content and system viscosity to obtain a high solid content, low viscosity UV-curable epoxy acrylate aqueous dispersion, which appeared as light yellow transparent mucus. Wherein, the degree of neutralization of the system is 70%, the solid content is 80%, and the amount of the polymerization inhibitor is 0.2% of the total mass of the maleic anhydride grafted epoxy acrylate prepolymer.
(4)向步骤(3)所得的环氧丙烯酸酯水分散体中加入活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯,光引发剂2-羟基-2-甲基-1-苯基-1-丙酮(光引发剂1173),搅拌均匀后涂膜,并于60℃烘箱中预烘30min,然后用2KW的紫外灯照射5s,得到环氧丙烯酸酯固化膜。其中,光引发剂用量为环氧丙烯酸酯水分散体和活性稀释剂总质量的4%,活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯与顺酐接枝环氧丙烯酸酯预聚物的质量比为1∶1∶8。(4) Add reactive diluent tripropylene glycol diacrylate and trimethylolpropane triacrylate in the epoxy acrylate aqueous dispersion of step (3) gained, photoinitiator 2-hydroxyl-2-methyl-1 -Phenyl-1-acetone (photoinitiator 1173), stir evenly, apply film, and pre-bake in an oven at 60°C for 30min, and then irradiate with 2KW UV lamp for 5s to obtain a cured epoxy acrylate film. Wherein, the amount of photoinitiator is 4% of the total mass of epoxy acrylate aqueous dispersion and reactive diluent, reactive diluent tripropylene glycol diacrylate and trimethylolpropane triacrylate and maleic anhydride grafted epoxy acrylate The mass ratio of the prepolymer is 1:1:8.
经检测,环氧稀释剂聚乙二醇二缩水甘油醚与环氧树脂E-51复配后体系从初始粘度6,220mPa·s降至65mPa·s,降粘率为98.88%;经过降粘改性的环氧丙烯酸酯预聚物的体系粘度从35,080mPa·s降至780mPa·s,降粘率为97.76%;再经顺丁烯二酸酐改性后的体系粘度为7,150mPa·s,而不经降粘改性的对应预聚物体系粘度高达100,000mPa·s以上。加水稀释至80%固含量时,水分散体的粘度降至2,650mPa.s,表明环氧稀释剂和部分水的加入大大降低了体系粘度。UV固化后涂膜的铅笔硬度为4H,附着力为1级,冲击性能为42Kg·cm,弯曲性能为2mm,表明固化膜有较高的硬度和很好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为12.70%。After testing, the compounding of epoxy diluent polyethylene glycol diglycidyl ether and epoxy resin E-51 reduced the initial viscosity from 6,220mPa·s to 65mPa·s, and the viscosity reduction rate was 98.88%. The viscosity of the epoxy acrylate prepolymer decreased from 35,080mPa·s to 780mPa·s, and the viscosity reduction rate was 97.76%; the viscosity of the system modified by maleic anhydride was 7,150mPa·s, while The viscosity of the corresponding prepolymer system without viscosity reduction modification is as high as 100,000mPa·s or more. When diluted with water to 80% solid content, the viscosity of the aqueous dispersion dropped to 2,650mPa.s, indicating that the addition of epoxy diluent and part of water greatly reduced the viscosity of the system. After UV curing, the pencil hardness of the coating film is 4H, the adhesion is grade 1, the impact performance is 42Kg·cm, and the bending performance is 2mm, indicating that the cured film has high hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 12.70%.
实施例4Example 4
(1)将46.26g环氧树脂E-51、38.95g数均分子量为550~750的聚丙二醇二缩水甘油醚、24.82g三羟甲基丙烷三缩水甘油醚和0.44g的阻聚剂对甲氧基苯酚,加入带有搅拌桨、温度计、恒压漏斗和冷凝管的四口反应烧瓶中;将35.26g丙烯酸装入恒压漏斗中。其中,环氧树脂E-51与聚丙二醇二缩水甘油醚和三羟甲基丙烷三缩水甘油醚中的环氧基团摩尔比为1∶0.5∶0.5,丙烯酸的羧基与环氧树脂复配体系的环氧基摩尔比为1∶1。待体系升温至75℃时,加入0.73g的催化剂N,N-二甲基苄胺,并开始滴加丙烯酸,0.5h滴加完毕。继续升温至85℃,反应至体系酸值<5mgKOH/g时结束,降温,得到降粘改性的环氧丙烯酸酯预聚物。阻聚剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚、三羟甲基丙烷三缩水甘油醚和丙烯酸总质量的0.3%;催化剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚、三羟甲基丙烷三缩水甘油醚和丙烯酸总质量的0.5%。(1) 46.26g of epoxy resin E-51, 38.95g of polypropylene glycol diglycidyl ether with a number average molecular weight of 550 to 750, 24.82g of trimethylolpropane triglycidyl ether and 0.44g of polymerization inhibitor Oxyphenol was added in a four-necked reaction flask with a stirring paddle, a thermometer, a constant pressure funnel and a condenser; 35.26g of acrylic acid was packed into the constant pressure funnel. Among them, the molar ratio of epoxy resin E-51 to polypropylene glycol diglycidyl ether and trimethylol propane triglycidyl ether is 1:0.5:0.5, and the carboxyl group of acrylic acid and epoxy resin compound system The epoxy group molar ratio is 1:1. When the temperature of the system was raised to 75°C, 0.73g of catalyst N,N-dimethylbenzylamine was added, and acrylic acid was added dropwise, and the dropwise addition was completed within 0.5h. Continue to raise the temperature to 85° C., the reaction ends when the acid value of the system is less than 5 mgKOH/g, and the temperature is lowered to obtain a viscosity-reduced modified epoxy acrylate prepolymer. The amount of polymerization inhibitor is 0.3% of the total mass of epoxy resin E-51, polypropylene glycol diglycidyl ether, trimethylolpropane triglycidyl ether and acrylic acid; the amount of catalyst is epoxy resin E-51, polypropylene glycol diglycidyl ether 0.5% of the total mass of glyceryl ether, trimethylolpropane triglycidyl ether and acrylic acid.
(2)待体系降温至60℃,加入28.40g顺酐、0.87g催化剂N,N-二甲基苄胺和0.52g阻聚剂对甲氧基苯酚,搅拌反应0.5h,然后升温至75℃,反应达理论酸值94.50mgKOH/g时降温,终止反应。其中,顺酐的摩尔用量为环氧丙烯酸酯预聚物的侧羟基摩尔含量的60%,催化剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.5%,阻聚剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.3%,理论酸值为顺酐与环氧丙烯酸酯预聚物发生半酯化后的体系酸值。(2) After the system cools down to 60°C, add 28.40g maleic anhydride, 0.87g catalyst N,N-dimethylbenzylamine and 0.52g polymerization inhibitor p-methoxyphenol, stir for 0.5h, then heat up to 75°C When the reaction reaches a theoretical acid value of 94.50mgKOH/g, the temperature is lowered to terminate the reaction. Wherein, the molar dosage of maleic anhydride is 60% of the side hydroxyl molar content of epoxy acrylate prepolymer, the catalyst dosage is 0.5% of the total mass of epoxy acrylate prepolymer and maleic anhydride, and the polymerization inhibitor dosage is epoxy acrylate 0.3% of the total mass of ester prepolymer and maleic anhydride, the theoretical acid value is the acid value of the system after maleic anhydride and epoxy acrylate prepolymer undergo half-esterification.
(3)待体系降温至50℃,加入0.35g阻聚剂对甲氧基苯酚和15.50g有机碱中和剂二甲氨基乙醇,进行中和反应。搅拌30min后加入126.13g去离子水调节固含量和体系粘度,得到高固含、低粘度的紫外光固化环氧丙烯酸酯水分散体,外观为浅黄色半透明胶体。其中,体系的中和度为60%,固含量为60%,阻聚剂用量为顺酐接枝环氧丙烯酸酯预聚物总质量的0.2%。(3) After the system cools down to 50°C, add 0.35g of polymerization inhibitor p-methoxyphenol and 15.50g of organic base neutralizing agent dimethylaminoethanol to carry out neutralization reaction. After stirring for 30 minutes, 126.13 g of deionized water was added to adjust the solid content and system viscosity to obtain a high solid content, low viscosity UV-curable epoxy acrylate aqueous dispersion, which appeared as a light yellow translucent colloid. Wherein, the degree of neutralization of the system is 60%, the solid content is 60%, and the amount of the polymerization inhibitor is 0.2% of the total mass of the maleic anhydride grafted epoxy acrylate prepolymer.
(4)向步骤(3)所得的环氧丙烯酸酯水分散体中加入活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯,光引发剂1-羟基-环己基-苯基甲酮(光引发剂184),搅拌均匀后涂膜,并于60℃烘箱中预烘40min,然后用2KW的紫外灯照射5s,得到环氧丙烯酸酯固化膜。其中,光引发剂用量为环氧丙烯酸酯水分散体和活性稀释剂总质量的4%,活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯与顺酐接枝环氧丙烯酸酯预聚物的质量比为1∶1∶8。(4) Add reactive diluent tripropylene glycol diacrylate and trimethylolpropane triacrylate in the epoxy acrylate aqueous dispersion of step (3) gained, photoinitiator 1-hydroxyl-cyclohexyl-phenylmethanol Ketone (photoinitiator 184), stir evenly and apply a film, and pre-baked in an oven at 60°C for 40 minutes, and then irradiated with a 2KW ultraviolet lamp for 5s to obtain a cured epoxy acrylate film. Wherein, the amount of photoinitiator is 4% of the total mass of epoxy acrylate aqueous dispersion and reactive diluent, reactive diluent tripropylene glycol diacrylate and trimethylolpropane triacrylate and maleic anhydride grafted epoxy acrylate The mass ratio of the prepolymer is 1:1:8.
经检测,环氧稀释剂聚丙二醇二缩水甘油醚、三羟甲基丙烷三缩水甘油醚与环氧树脂E-51复配后体系从初始粘度6,220mPa·s降至350mPa·s,降粘率为94.37%;经过降粘改性的环氧丙烯酸酯预聚物的体系粘度从35,080mPa·s降至3,120mPa·s,降粘率为91.11%;再经顺丁烯二酸酐改性后的体系粘度为32,610mPa·s,而不经降粘改性的对应预聚物体系粘度高达100,000mPa·s以上。加水稀释至60%固含量时,水分散体的粘度降至2,950mPa.s。可见,虽然加入三官能度的环氧稀释剂三羟甲基丙烷三缩水甘油醚会提高预聚物体系的粘度,但稀释至更低固含量后,仍可将粘度降至3000mPa.s以下。UV固化后涂膜的铅笔硬度为6H,附着力为2级,冲击性能为33Kg·cm,弯曲性能为4mm,表明固化膜有很高的硬度和较好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为8.90%。After testing, the epoxy diluent polypropylene glycol diglycidyl ether, trimethylolpropane triglycidyl ether and epoxy resin E-51 compounded the system from the initial viscosity of 6,220mPa s to 350mPa s, and the viscosity reduction rate was 94.37%; the viscosity of the epoxy acrylate prepolymer modified by viscosity reduction dropped from 35,080mPa·s to 3,120mPa·s, and the viscosity reduction rate was 91.11%; and then modified by maleic anhydride The viscosity of the system is 32,610mPa·s, while the viscosity of the corresponding prepolymer system without viscosity reduction modification is as high as 100,000mPa·s or more. When diluted with water to 60% solid content, the viscosity of the aqueous dispersion dropped to 2,950 mPa.s. It can be seen that although the addition of the trifunctional epoxy diluent trimethylolpropane triglycidyl ether will increase the viscosity of the prepolymer system, after dilution to a lower solid content, the viscosity can still be reduced to below 3000mPa.s. After UV curing, the pencil hardness of the coating film is 6H, the adhesion is grade 2, the impact performance is 33Kg·cm, and the bending performance is 4mm, indicating that the cured film has high hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 8.90%.
实施例5Example 5
(1)将46.26g环氧树脂E-51、77.86g数均分子量为550~750的聚丙二醇二缩水甘油醚和0.48g的阻聚剂2,6-二叔丁基对甲酚,加入带有搅拌桨、温度计、恒压漏斗和冷凝管的四口反应烧瓶中;将35.26g丙烯酸装入恒压漏斗中。其中,环氧树脂E-51与聚丙二醇二缩水甘油醚中的环氧基团摩尔比为1∶1,丙烯酸的羧基与环氧树脂复配体系的环氧基摩尔比为1∶1。待体系升温至75℃时,加入0.80g的催化剂N,N-二甲基苄胺,并开始滴加丙烯酸,0.5h滴加完毕。继续升温至85℃,反应至体系酸值<5mgKOH/g时结束,降温,得到降粘改性的环氧丙烯酸酯预聚物。阻聚剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚和丙烯酸总质量的0.3%;催化剂用量为环氧树脂E-51、聚丙二醇二缩水甘油醚和丙烯酸总质量的0.5%。(1) 46.26g of epoxy resin E-51, 77.86g of polypropylene glycol diglycidyl ether with a number average molecular weight of 550 to 750 and 0.48g of polymerization inhibitor 2,6-di-tert-butyl p-cresol were added with In a four-necked reaction flask with a stirring paddle, a thermometer, a constant pressure funnel and a condenser; 35.26g of acrylic acid was charged into the constant pressure funnel. Among them, the molar ratio of epoxy resin E-51 and epoxy group in polypropylene glycol diglycidyl ether is 1:1, and the molar ratio of carboxyl group of acrylic acid and epoxy resin compound system is 1:1. When the temperature of the system was raised to 75° C., 0.80 g of catalyst N,N-dimethylbenzylamine was added, and acrylic acid was added dropwise, and the dropwise addition was completed within 0.5 h. Continue to raise the temperature to 85° C., the reaction ends when the acid value of the system is less than 5 mgKOH/g, and the temperature is lowered to obtain a viscosity-reduced modified epoxy acrylate prepolymer. The amount of polymerization inhibitor is 0.3% of the total mass of epoxy resin E-51, polypropylene glycol diglycidyl ether and acrylic acid; the amount of catalyst is 0.5% of the total mass of epoxy resin E-51, polypropylene glycol diglycidyl ether and acrylic acid.
(2)待体系降温至60℃,加入18.94g顺酐、0.89g催化剂N,N-二甲基苄胺和0.53g阻聚剂2,6-二叔丁基对甲酚,搅拌反应0.5h,然后升温至75℃,反应达理论酸值75.80mgKOH/g时降温,终止反应。其中,顺酐的摩尔用量为环氧丙烯酸酯预聚物的侧羟基摩尔含量的40%,催化剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.5%,阻聚剂用量为环氧丙烯酸酯预聚物和顺酐总质量的0.3%,理论酸值为顺酐与环氧丙烯酸酯预聚物发生半酯化后的体系酸值。(2) After the system cools down to 60°C, add 18.94g maleic anhydride, 0.89g catalyst N,N-dimethylbenzylamine and 0.53g polymerization inhibitor 2,6-di-tert-butyl-p-cresol, and stir for 0.5h , and then the temperature was raised to 75°C, and the temperature was lowered when the reaction reached a theoretical acid value of 75.80 mgKOH/g to terminate the reaction. Wherein, the molar dosage of maleic anhydride is 40% of the side hydroxyl molar content of epoxy acrylate prepolymer, the catalyst dosage is 0.5% of the total mass of epoxy acrylate prepolymer and maleic anhydride, and the polymerization inhibitor dosage is epoxy acrylate 0.3% of the total mass of ester prepolymer and maleic anhydride, the theoretical acid value is the acid value of the system after maleic anhydride and epoxy acrylate prepolymer undergo half-esterification.
(3)待体系降温至50℃,加入0.36g阻聚剂2,6-二叔丁基对甲酚,将15.65g有机碱三乙胺与3.56g数均分子量为100的氨基硅油混合均匀制成中和剂,加入顺酐接枝环氧丙烯酸酯预聚物中进行中和反应。搅拌30min后加入49.38g去离子水,调节固含量和体系粘度,得到高固含、低粘度的紫外光固化环氧丙烯酸酯水分散体,外观为浅黄色半透明胶体。其中固含量为80%,体系的有机碱中和度为80%,氨基硅油占顺酐接枝环氧丙烯酸酯预聚物总质量的2.0%,阻聚剂用量为顺酐接枝环氧丙烯酸酯预聚物总质量的0.2%。(3) After the system cools down to 50°C, add 0.36g of polymerization inhibitor 2,6-di-tert-butyl-p-cresol, mix 15.65g of organic base triethylamine and 3.56g of amino silicone oil with a number average molecular weight of 100 to prepare It can be used as a neutralizing agent and added to the maleic anhydride grafted epoxy acrylate prepolymer for neutralization reaction. After stirring for 30 minutes, 49.38 g of deionized water was added to adjust the solid content and system viscosity to obtain a high solid content, low viscosity UV-curable epoxy acrylate aqueous dispersion, which appeared as a light yellow translucent colloid. Wherein the solid content is 80%, the organic base neutralization degree of the system is 80%, the amino silicone oil accounts for 2.0% of the total mass of the maleic anhydride grafted epoxy acrylate prepolymer, and the amount of the polymerization inhibitor is maleic anhydride grafted epoxy acrylate 0.2% of the total mass of the ester prepolymer.
(4)向步骤(3)所得的有机硅改性环氧丙烯酸酯预聚物中加入活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯,光引发剂1-羟基-环己基-苯基甲酮(光引发剂184),搅拌均匀后涂膜,并于60℃烘箱中预烘30min,然后用2KW的紫外灯照射5s,得到环氧丙烯酸酯固化膜。其中,光引发剂用量为有机硅改性环氧丙烯酸酯预聚物和活性稀释剂总质量的4%,活性稀释剂三丙二醇二丙烯酸酯和三羟甲基丙烷三丙烯酸酯与顺酐接枝环氧丙烯酸酯预聚物的质量比为1∶1∶8。(4) Add reactive diluent tripropylene glycol diacrylate and trimethylol propane triacrylate in the organosilicon-modified epoxy acrylate prepolymer of step (3) gained, photoinitiator 1-hydroxyl-cyclohexyl -Phenyl ketone (photoinitiator 184), after stirring evenly, coat the film, pre-bake it in an oven at 60°C for 30 minutes, and then irradiate it with a 2KW ultraviolet lamp for 5 seconds to obtain a cured epoxy acrylate film. Wherein, the amount of photoinitiator is 4% of the total mass of organosilicon-modified epoxy acrylate prepolymer and reactive diluent, reactive diluent tripropylene glycol diacrylate and trimethylolpropane triacrylate and maleic anhydride graft The mass ratio of the epoxy acrylate prepolymer is 1:1:8.
与实施例1和2相比,本例中的环氧丙烯酸酯预聚物经有机硅改性后体系粘度从10,840mPa·s增加到18,540mPa·s。加水稀释至80%固含量时,水分散体的粘度又降至5,270mPa.s,表明环氧稀释剂的加入大大降低了体系粘度。UV固化后涂膜的铅笔硬度为5H,附着力为2级,冲击性能为38Kg·cm,弯曲性能为3mm,表明固化膜有较高的硬度和良好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为3.05%,显示出优异的耐水性。Compared with Examples 1 and 2, the viscosity of the epoxy acrylate prepolymer in this example increased from 10,840 mPa·s to 18,540 mPa·s after silicone modification. When diluted with water to 80% solid content, the viscosity of the aqueous dispersion dropped to 5,270mPa.s, indicating that the addition of epoxy diluent greatly reduced the viscosity of the system. After UV curing, the pencil hardness of the coating film is 5H, the adhesion is grade 2, the impact performance is 38Kg·cm, and the bending performance is 3mm, indicating that the cured film has high hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 3.05%, showing excellent water resistance.
实施例6Example 6
与实施例5反应过程基本相同。其中,步骤(3)中的15.65g有机碱三乙胺与3.56g数均分子量为100的氨基硅油改用17.60g有机碱三乙胺与1.78g数均分子量为100的氨基硅油,其他原料的相应配比保持不变,用量作相应调整。The reaction process is basically the same as in Example 5. Wherein, 15.65g organic base triethylamine and 3.56g number average molecular weight in step (3) are the amino silicone oil of 100 with 17.60g organic base triethylamine and 1.78g number average molecular weight being the amino silicone oil of 100, other raw materials The corresponding ratio remains unchanged, and the dosage is adjusted accordingly.
与实施例5相比,本例中的环氧丙烯酸酯预聚物经有机硅改性后体系粘度从10,840mPa·s增加至13,100mPa·s。加水稀释至80%固含量时,水分散体的粘度降至3,250mPa.s。UV固化后涂膜的铅笔硬度为5H,附着力为1级,冲击性能为43Kg·cm,弯曲性能为2mm,表明固化膜有较高的硬度和良好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为3.90%,显示出优异的耐水性。Compared with Example 5, the viscosity of the epoxy acrylate prepolymer in this example increased from 10,840 mPa·s to 13,100 mPa·s after silicone modification. When diluted with water to 80% solid content, the viscosity of the aqueous dispersion drops to 3,250 mPa.s. After UV curing, the pencil hardness of the coating film is 5H, the adhesion is grade 1, the impact performance is 43Kg·cm, and the bending performance is 2mm, indicating that the cured film has high hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 3.90%, showing excellent water resistance.
实施例7Example 7
与实施例6反应过程基本相同。其中,步骤(1)中的46.26g环氧树脂E-51改用44.69g环氧树脂E-54,其他原料的相应配比保持不变,用量作相应调整。The reaction process is basically the same as in Example 6. Wherein, 46.26g epoxy resin E-51 in the step (1) is replaced with 44.69g epoxy resin E-54, and the corresponding proportioning of other raw materials remains unchanged, and consumption is adjusted accordingly.
与实施例6相比,本例中的环氧丙烯酸酯预聚物经有机硅改性后体系粘度从7,350mPa·s增加至8,620mPa·s。加水稀释至80%固含量时,水分散体的粘度降至2,100mPa.s,表明环氧树脂E-54的起始粘度较低,最终合成的有机硅改性环氧丙烯酸酯水分散体的粘度可低至2,000mPa.s左右。UV固化后涂膜的铅笔硬度为6H,附着力为2级,冲击性能为40Kg·cm,弯曲性能为3mm,表明固化膜有更高的硬度和良好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为3.30%,显示出优异的耐水性。Compared with Example 6, the viscosity of the epoxy acrylate prepolymer in this example increased from 7,350 mPa·s to 8,620 mPa·s after silicone modification. When diluted with water to 80% solid content, the viscosity of the aqueous dispersion dropped to 2,100mPa.s, indicating that the initial viscosity of epoxy resin E-54 was low, and the final synthetic silicone modified epoxy acrylate aqueous dispersion The viscosity can be as low as about 2,000mPa.s. After UV curing, the pencil hardness of the coating film is 6H, the adhesion is grade 2, the impact performance is 40Kg·cm, and the bending performance is 3mm, indicating that the cured film has higher hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 3.30%, showing excellent water resistance.
实施例8Example 8
与实施例6反应过程基本相同。其中,步骤(1)中的46.26g环氧树脂E-51改用54.96g环氧树脂E-44,其他原料的相应配比保持不变,用量作相应调整。The reaction process is basically the same as in Example 6. Wherein, the 46.26g epoxy resin E-51 in the step (1) is replaced with 54.96g epoxy resin E-44, and the corresponding proportioning of other raw materials remains unchanged, and consumption is adjusted accordingly.
与实施例6相比,本例中的环氧丙烯酸酯预聚物经有机硅改性后体系粘度从21,540mPa·s增加至25,060mPa·s。加水稀释至80%固含量时,水分散体的粘度降至9,850mPa.s,表明环氧树脂E-44的起始粘度较高,最终合成的有机硅改性环氧丙烯酸酯水分散体的粘度仍接近10,000mPa.s左右。加水稀释至60%固含量时,水分散体的粘度可降至4,120mPa.s。UV固化后涂膜的铅笔硬度为4H,附着力为1级,冲击性能为48Kg·cm,弯曲性能为1mm,表明固化膜有较高的硬度和良好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为4.60%,显示出优异的耐水性。Compared with Example 6, the viscosity of the epoxy acrylate prepolymer in this example increased from 21,540 mPa·s to 25,060 mPa·s after silicone modification. When diluted with water to 80% solid content, the viscosity of the aqueous dispersion dropped to 9,850mPa.s, indicating that the initial viscosity of epoxy resin E-44 was higher, and the final synthetic silicone modified epoxy acrylate aqueous dispersion The viscosity is still close to about 10,000mPa.s. When diluted with water to 60% solid content, the viscosity of the aqueous dispersion can be reduced to 4,120mPa.s. After UV curing, the pencil hardness of the coating film is 4H, the adhesion is grade 1, the impact performance is 48Kg·cm, and the bending performance is 1mm, indicating that the cured film has high hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), and the water absorption rate is 4.60%, showing excellent water resistance.
实施例9Example 9
与实施例8反应过程相同。其中,步骤(1)中的54.96g环氧树脂E-44和77.86g数均分子量为550~750的聚丙二醇二缩水甘油醚改用36.39g环氧树脂E-44和103.59g数均分子量为550~750的聚丙二醇二缩水甘油醚,即环氧树脂E-44与聚丙二醇二缩水甘油醚中的环氧基团摩尔比由1∶1改为1∶2,其他原料的相应配比保持不变,用量作相应调整。Same as embodiment 8 reaction process. Wherein, 54.96g epoxy resin E-44 and 77.86g number average molecular weight in the step (1) are 550~750 polypropylene glycol diglycidyl ethers and use 36.39g epoxy resin E-44 and 103.59g number average molecular weight to be 550-750 polypropylene glycol diglycidyl ether, that is, the molar ratio of epoxy resin E-44 to epoxy group in polypropylene glycol diglycidyl ether is changed from 1:1 to 1:2, and the corresponding ratio of other raw materials remains No change, the dosage is adjusted accordingly.
与实施例8相比,本例中的有机硅改性环氧丙烯酸酯预聚物的体系粘度从25,060mPa·s降低至12,160mPa·s。加水稀释至80%固含量时,水分散体的粘度降至3,510mPa.s,表明增加聚丙二醇二缩水甘油醚的用量可以大幅降低有机硅改性环氧丙烯酸酯水分散体的粘度。UV固化后涂膜的铅笔硬度为4H,附着力为1级,冲击性能为50Kg·cm,弯曲性能为1mm,表明固化膜有较高的硬度和良好的柔韧性。固化膜在25℃蒸馏水中浸泡24h后无变化(不变色、不起泡、不脱落),吸水率为4.85%,依然具有优异的耐水性。Compared with Example 8, the system viscosity of the silicone-modified epoxy acrylate prepolymer in this example decreased from 25,060 mPa·s to 12,160 mPa·s. When diluted with water to 80% solid content, the viscosity of the aqueous dispersion dropped to 3,510mPa.s, indicating that increasing the amount of polypropylene glycol diglycidyl ether can greatly reduce the viscosity of the silicone-modified epoxy acrylate aqueous dispersion. After UV curing, the pencil hardness of the coating film is 4H, the adhesion is grade 1, the impact performance is 50Kg·cm, and the bending performance is 1mm, indicating that the cured film has high hardness and good flexibility. The cured film has no change after soaking in distilled water at 25°C for 24 hours (no discoloration, no foaming, no falling off), the water absorption rate is 4.85%, and it still has excellent water resistance.
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