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CN108976425A - A kind of preparation method of polyurethane-epoxy resin block copolymerization water-base resin - Google Patents

A kind of preparation method of polyurethane-epoxy resin block copolymerization water-base resin Download PDF

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CN108976425A
CN108976425A CN201810615076.3A CN201810615076A CN108976425A CN 108976425 A CN108976425 A CN 108976425A CN 201810615076 A CN201810615076 A CN 201810615076A CN 108976425 A CN108976425 A CN 108976425A
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epoxy resin
polyurethane
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epoxy
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CN108976425B (en
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邓剑如
江维胜
张旭东
黄鹂
李健
刘娅莉
刘美凤
任艳群
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HUNAN KANSAI AUTOMOTIVE COATINGS CO Ltd
Hunan University
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Hunan University
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G81/00Macromolecular compounds obtained by interreacting polymers in the absence of monomers, e.g. block polymers
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/44Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications
    • C09D5/4419Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications with polymers obtained otherwise than by polymerisation reactions only involving carbon-to-carbon unsaturated bonds
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/44Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications
    • C09D5/4419Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications with polymers obtained otherwise than by polymerisation reactions only involving carbon-to-carbon unsaturated bonds
    • C09D5/4465Polyurethanes

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Abstract

A kind of preparation method of polyurethane-epoxy resin block copolymerization water-base resin, comprising the following steps: (1) oligomer dihydric alcohol and di-isocyanate reaction are obtained into base polyurethane prepolymer for use as;(2) epoxy resin, piperazine and water-soluble solvent is added, reaction to epoxide number is 0, obtains mixture;(3) deionized water with quality such as added water-soluble solvents is added, stirs evenly, then staticly settle out polymer, washes polymer, obtains precursor resin;(4) gained precursor resin is heated up, be added organic acid, stirring, be added deionized water, stir 20-35min to get.The present invention realizes the block copolymerization of polyurethane resin and epoxy resin, overcomes limitation of the synthetic method of common polyurethane epoxy material to epoxy resin introduction volume;And the present invention can adjust the performance of products obtained therefrom by adjusting formulation parameter.

Description

一种聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法A kind of preparation method of polyurethane-epoxy resin block copolymerization waterborne resin

技术领域technical field

本发明涉及聚氨酯-环氧树脂材料领域,具体来说涉及一种聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法,其特别适于作阴极电泳涂料。The invention relates to the field of polyurethane-epoxy resin materials, in particular to a method for preparing a polyurethane-epoxy resin block copolymerized water-based resin, which is particularly suitable for cathodic electrophoretic coatings.

背景技术Background technique

环氧树脂种类繁多,应用领域广泛。然而未经改性的环氧树脂固化后交联密度高,导致内应力过大,产品存在质脆、易开裂、耐冲击性差等缺陷,限制了其应用领域。而聚氨酯具有良好的柔韧性,以其与环氧树脂共聚改性,可以做到优势互补,获得使用性能更加优异的聚氨酯环氧材料。通常制备聚氨酯环氧材料的方法有机械共混法、直接接枝共聚法及环氧开环法等三种方法。There are many kinds of epoxy resins and their application fields are wide. However, the unmodified epoxy resin has high crosslinking density after curing, resulting in excessive internal stress, and the product has defects such as brittleness, easy cracking, and poor impact resistance, which limit its application field. Polyurethane has good flexibility, and its copolymerization modification with epoxy resin can achieve complementary advantages and obtain polyurethane epoxy materials with better performance. There are usually three methods for preparing polyurethane epoxy materials: mechanical blending method, direct graft copolymerization method and epoxy ring-opening method.

机械共混法是用亲水性的聚氨酯预聚体包裹环氧树脂,然后水化,得到环氧改性聚氨酯树脂乳液。该方法的优点是,易制备出稳定的树脂乳液,但有两处不足的之处,其一,该方法只是物理上的简单共混,两种树脂并没有化学键的链接,因此,不能很好的使两种树脂的优势互补,从而很难得到性能优良的漆膜;其二,环氧树脂是通过被包裹才能稳定的分散到乳液中,因此,环氧树脂增多,得到的树脂乳液粒径变大,甚至部分环氧树脂无法被包覆,影响树脂乳液的稳定性,导致只能用较少的环氧树脂改性聚氨酯,从而影响了产品的应用范围。The mechanical blending method is to wrap the epoxy resin with a hydrophilic polyurethane prepolymer, and then hydrate it to obtain an epoxy-modified polyurethane resin emulsion. The advantage of this method is that it is easy to prepare a stable resin emulsion, but there are two disadvantages. First, the method is simply a physical blend, and the two resins do not have chemical bonds. The advantages of the two resins complement each other, so it is difficult to obtain a paint film with excellent performance; secondly, the epoxy resin can be stably dispersed into the emulsion by being wrapped, so the increase in the epoxy resin increases the particle size of the obtained resin emulsion. become larger, and even part of the epoxy resin cannot be coated, which affects the stability of the resin emulsion, resulting in the use of less epoxy resin to modify polyurethane, thus affecting the application range of the product.

直接接枝共聚法是先合成出聚氨酯预聚体,然后预聚体和环氧树脂中的仲羟基反应,将聚氨酯引入到环氧树脂中。该方法的优点是,得到的漆膜各项性能优于机械共混法得到的漆膜,缺点是较难制备出稳定的树脂乳液,因为在聚合反应中,环氧树脂参与反应后会产生支化链,因此,其用量超过一定范围时,会使反应物的分子量急剧增大,导致树脂很难被水化或者得不到稳定的乳液。The direct graft copolymerization method is to synthesize a polyurethane prepolymer first, and then the prepolymer reacts with the secondary hydroxyl groups in the epoxy resin to introduce polyurethane into the epoxy resin. The advantage of this method is that the properties of the obtained paint film are better than those obtained by the mechanical blending method. The disadvantage is that it is difficult to prepare a stable resin emulsion, because in the polymerization reaction, epoxy resin will produce branches after participating in the reaction. Therefore, when the amount exceeds a certain range, the molecular weight of the reactant will increase sharply, making it difficult for the resin to be hydrated or to obtain a stable emulsion.

环氧开环法是先利用小分子酸、胺或醇等与环氧树脂进行开环反应,生成端羟基环氧树脂,然后将其作为一种多元醇与二异氰酸酯反应。该方法制提升了环氧树脂的用量,制备得到的漆膜性能优异。但是不足的地方是,环氧树脂开环的反应过程较难控制且不能完全开环,因此,得到的改性树脂乳液中含有环氧基和小分子开环剂(如酸、胺等),影响乳液的存储稳定性。The epoxy ring-opening method is to use a small molecular acid, amine or alcohol to perform a ring-opening reaction with an epoxy resin to generate a hydroxyl-terminated epoxy resin, and then react it as a polyol with a diisocyanate. The method increases the amount of epoxy resin used, and the prepared paint film has excellent performance. However, the disadvantage is that the ring-opening reaction process of epoxy resin is difficult to control and cannot be completely opened. Therefore, the obtained modified resin emulsion contains epoxy groups and small molecule ring-opening agents (such as acids, amines, etc.), affect the storage stability of the emulsion.

发明内容Contents of the invention

本发明要解决的技术问题是,克服现有技术的不足,提供一种工艺较简单的聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法,所得聚氨酯-环氧树脂嵌段共聚水性树脂存储稳定性较好。The technical problem to be solved in the present invention is to overcome the deficiencies in the prior art and provide a method for preparing a polyurethane-epoxy resin block copolymerized water-based resin with a relatively simple process, and the obtained polyurethane-epoxy resin block copolymerized water-based resin is stable in storage sex is better.

本发明解决其技术问题采用的技术方案是,一种聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法,包括以下步骤:The technical scheme that the present invention solves its technical problem adopts is, a kind of preparation method of polyurethane-epoxy resin block copolymerization waterborne resin, comprises the following steps:

(1)将低聚物二元醇和二异氰酸酯投入反应瓶中,反应温度为50℃~80℃,反应1~3h,制备得到聚氨酯预聚体;(1) Put the oligomer diol and diisocyanate into the reaction bottle, the reaction temperature is 50°C~80°C, and react for 1~3h to prepare the polyurethane prepolymer;

所述低聚物二元醇和二异氰酸酯的比例,应使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为1.5-2︰1;The ratio of the oligomer dibasic alcohol and diisocyanate should make the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 1.5-2:1;

(2)往步骤(1)所得聚氨酯预聚体中加入环氧树脂、哌嗪和水溶性溶剂,搅拌均匀,升温至30℃~70℃,反应3~8 h,反应至环氧值为0,得混合物;(2) Add epoxy resin, piperazine and water-soluble solvent to the polyurethane prepolymer obtained in step (1), stir evenly, raise the temperature to 30°C~70°C, and react for 3~8 hours until the epoxy value is 0 , to get a mixture;

所述水溶性溶剂的加入量,为聚氨酯预聚体、环氧树脂、哌嗪总质量的60-100%;The addition of the water-soluble solvent is 60-100% of the total mass of polyurethane prepolymer, epoxy resin, and piperazine;

环氧树脂和哌嗪的配比,以扩链参数Rt和硬段含量H%来控制;The ratio of epoxy resin and piperazine is controlled by chain extension parameter Rt and hard segment content H%;

控制扩链参数Rt=1.2~1.6, Rt ={n(氨基)/ [ n(环氧基)+n(异氰酸酯基)]},n表示物质的量(摩尔数)。Rt控制在此范围,可以控制合成树脂的分子量,一般Rt>1.0,确保嵌段共聚物以胺基封端;氨基为哌嗪中的仲胺,环氧基为环氧树脂中的环氧基,异氰酸酯基为聚氨酯预聚体中的异氰酸酯基。Control the chain extension parameter Rt=1.2~1.6, Rt={n(amino group)/[n(epoxy group)+n(isocyanate group)]}, n represents the amount of substance (number of moles). Controlling Rt within this range can control the molecular weight of the synthetic resin. Generally, Rt>1.0 ensures that the block copolymer is terminated with an amine group; the amino group is the secondary amine in piperazine, and the epoxy group is the epoxy group in the epoxy resin. , The isocyanate group is the isocyanate group in the polyurethane prepolymer.

控制硬段含量H%为10~60%(优选20-50%); H%={[ m(环氧树脂)+m(哌嗪)]/ [ m(环氧树脂)+m(哌嗪)+ m(聚氨酯预聚体)] },m表示物质的质量。硬段含量H%为硬段含量,可以调节合成树脂的柔韧性。Control the hard segment content H% to be 10~60% (preferably 20-50%); H%={[m(epoxy resin)+m(piperazine)]/ [m(epoxy resin)+m(piperazine) )+ m (polyurethane prepolymer)] }, m represents the quality of the substance. The hard segment content H% is the hard segment content, which can adjust the flexibility of the synthetic resin.

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至40-55℃,加入相当于前驱树脂质量1.2~16.0%(优选2.8-10.0%)的有机酸,搅拌3-10min,加入相当于前驱树脂质量1-3倍的去离子水,搅拌20-35min(乳化),即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Raise the temperature of the precursor resin obtained in step (3) to 40-55°C, add an organic acid equivalent to 1.2-16.0% (preferably 2.8-10.0%) of the mass of the precursor resin, stir for 3-10 minutes, and add an organic acid equivalent to the mass of the precursor resin 1-3 times the amount of deionized water, stirred for 20-35min (emulsification), and the polyurethane-epoxy resin block copolymerized water-based resin was obtained.

进一步,步骤(1)中,所述低聚物二元醇为聚己内酯二元醇、聚己二酸一缩二乙二醇酯、聚四氢呋喃二元醇中的至少一种,其中优选聚己内酯二元醇。Further, in step (1), the oligomer diol is at least one of polycaprolactone diol, polyethylene adipate, and polytetrahydrofuran diol, among which preferably Polycaprolactone diol.

进一步,步骤(1)中,所述低聚物二元醇分子量为400-4000,其中优选分子量为1000-2000。Further, in step (1), the molecular weight of the oligomer diol is 400-4000, wherein the preferred molecular weight is 1000-2000.

进一步,步骤(1)中,所述二异氰酸酯为甲苯二异氰酸酯(TDI)、异佛尔酮二异氰酸酯(IPDI)、二苯基甲烷二异氰酸酯(MDI)、六亚甲基二异氰酸酯(HDI)中的至少一种,其中优选甲苯二异氰酸酯(TDI)、异佛尔酮二异氰酸酯(IPDI)中的至少一种。Further, in step (1), the diisocyanate is toluene diisocyanate (TDI), isophorone diisocyanate (IPDI), diphenylmethane diisocyanate (MDI), hexamethylene diisocyanate (HDI) At least one of, among which at least one of toluene diisocyanate (TDI) and isophorone diisocyanate (IPDI) is preferred.

进一步,步骤(2)中,所述环氧树脂为环氧E-51、环氧E-44、环氧E-20、环氧E-12中的至少一种,优选环氧E-44、E-20。环氧值越低,则水性树脂中的胺值越小。Further, in step (2), the epoxy resin is at least one of epoxy E-51, epoxy E-44, epoxy E-20, epoxy E-12, preferably epoxy E-44, E-20. The lower the epoxy value, the smaller the amine value in the water-based resin.

进一步,步骤(2)中,所述水溶性溶剂为N,N-二甲基甲酰胺、四氢呋喃、丙酮、N-甲基吡咯烷酮中的一种或两种,其中优选N,N-二甲基甲酰胺、四氢呋喃中的至少一种。Further, in step (2), the water-soluble solvent is one or both of N,N-dimethylformamide, tetrahydrofuran, acetone, and N-methylpyrrolidone, among which N,N-dimethyl At least one of formamide and tetrahydrofuran.

反应中加入水溶性溶剂,其原因有以下三点:其一,溶解反应物,使反应物分子充分接触,从而反应更加充分;其二,能够降低反应体系的粘度,有利于体系的传热和散热;其三,其为水溶性溶剂,故反应停止后,只需加入去离子水便可沉淀出前驱树脂,而溶剂与水的混合液,仅需经简单蒸馏脱水,便可回收利用,因此,免去了一般水性树脂制备过程中脱除溶剂的步骤。There are three reasons for adding a water-soluble solvent to the reaction: first, it dissolves the reactant, and makes the reactant molecules fully contact, so that the reaction is more complete; second, it can reduce the viscosity of the reaction system, which is beneficial to the heat transfer and Heat dissipation; third, it is a water-soluble solvent, so after the reaction is stopped, only need to add deionized water to precipitate the precursor resin, and the mixture of solvent and water can be recycled after simple distillation and dehydration, so , eliminating the step of solvent removal in the general water-based resin preparation process.

进一步,步骤(2)中,控制反应为温度45-60℃。Further, in step (2), the reaction is controlled at a temperature of 45-60°C.

进一步,步骤(2)中,控制反应时间为4-6h。Further, in step (2), the reaction time is controlled to be 4-6h.

进一步,步骤(4)中,所述有机酸为冰醋酸、乳酸、甲酸、丙酸、草酸等中的至少一种。Further, in step (4), the organic acid is at least one of glacial acetic acid, lactic acid, formic acid, propionic acid, oxalic acid and the like.

本发明的设计原理:以低聚物二元醇和二异氰酸酯合成聚氨酯预聚体,将其与哌嗪及环氧树脂进行扩链聚合反应,通过控制共聚物的物料配比来调节合成树脂的分子量和柔韧性,制备系列线型多嵌段大分子树脂。The design principle of the present invention: Synthesize polyurethane prepolymer with oligomer diol and diisocyanate, carry out chain extension polymerization reaction with piperazine and epoxy resin, adjust the molecular weight of synthetic resin by controlling the material ratio of copolymer and flexibility to prepare a series of linear multi-block macromolecular resins.

本发明采用哌嗪扩链的目的有如下两点:①哌嗪是环状结构物质,用其扩链改性,能提高合成树脂膜的强度;②哌嗪两端是仲胺基,用其扩链有如下两点优势,其一,给合成树脂引入可被离子化胺基的同时,使树脂的胺值在较低的范围。其二,它在较低的温度下可与异氰酸酯基、环氧基反应,其速度远大于环氧上仲羟基与异氰酸酯基的反应速度,因此,反应工艺简单、经济。The present invention adopts the purpose of piperazine chain extension to have the following two points: 1. piperazine is a cyclic structure material, which can be modified by chain extension to improve the strength of synthetic resin film; 2. piperazine two ends are secondary amino groups, and its Chain extension has the following two advantages. First, while introducing ionizable amine groups into the synthetic resin, the amine value of the resin is kept in a lower range. Second, it can react with isocyanate groups and epoxy groups at a lower temperature, and its speed is much faster than the reaction speed of secondary hydroxyl groups on epoxy and isocyanate groups. Therefore, the reaction process is simple and economical.

本发明采用聚氨酯预聚体扩链的目的有如下三点:①聚氨酯预聚体两端为异氰酸酯基,可以在较低的温度下与哌嗪中的仲氨基反应;②聚氨酯预聚体的引入可以使合成出的树脂有一定的柔韧性;③聚氨酯预聚体中含有疏水性的链段,可以包覆封闭型异氰酸酯固化剂,从而能使固化剂与树脂同步成比例地电泳至电极表面。The purpose of chain extension of polyurethane prepolymer used in the present invention has the following three points: 1. the two ends of polyurethane prepolymer are isocyanate groups, which can react with the secondary amino group in piperazine at a lower temperature; 2. the introduction of polyurethane prepolymer It can make the synthesized resin have certain flexibility; ③The polyurethane prepolymer contains a hydrophobic segment, which can cover the blocked isocyanate curing agent, so that the curing agent and the resin can be electrophoresed to the surface of the electrode synchronously and proportionally.

本发明以环氧树脂为硬段,聚氨酯预聚体为软段,以哌嗪为扩链剂,通过调节扩链参数(Rt)来控制合成树脂的分子量,通过调节硬段含量(H%)来调节合成树脂的柔韧性,精准制备系列聚氨酯-环氧树脂线型嵌段共聚物,经中和水化,获得系列聚氨酯-环氧树脂嵌段共聚水性树脂,也可将合成的前驱树脂与封闭型异氰酸酯复配,制成阴极电泳涂料。In the present invention, epoxy resin is used as the hard segment, polyurethane prepolymer is used as the soft segment, piperazine is used as the chain extender, and the molecular weight of the synthetic resin is controlled by adjusting the chain extension parameter (Rt). By adjusting the hard segment content (H%) To adjust the flexibility of the synthetic resin, a series of polyurethane-epoxy resin linear block copolymers are precisely prepared, and after neutralization and hydration, a series of polyurethane-epoxy resin block copolymerization water-based resins can be obtained. The synthetic precursor resin can also be combined with Compounded with blocked isocyanate to make cathodic electrophoretic coating.

本发明之聚氨酯-环氧树脂嵌段共聚水性树脂制备过程反应式如下:The reaction formula of the preparation process of the polyurethane-epoxy resin block copolymerized water-based resin of the present invention is as follows:

与现有技术相比,本发明优势如下:Compared with the prior art, the present invention has the following advantages:

(1)本发明以环氧树脂为硬段,聚氨酯预聚体为软段,以哌嗪为扩链剂,通过调节扩链参数来控制合成树脂的分子量,通过调节硬段含量来调节合成出树脂的柔韧性。这种合成方法实现了聚氨酯树脂和环氧树脂的嵌段共聚,克服了常用聚氨酯环氧树脂材料的合成方法对环氧树脂引入量的限制;而且本发明可以通过调节共聚物的物料配比来调节所得产品的性能。(1) In the present invention, epoxy resin is used as the hard segment, polyurethane prepolymer is used as the soft segment, piperazine is used as the chain extender, the molecular weight of the synthetic resin is controlled by adjusting the chain extension parameters, and the synthetic resin is adjusted by adjusting the content of the hard segment. The flexibility of the resin. This synthetic method has realized the block copolymerization of polyurethane resin and epoxy resin, has overcome the synthetic method of common polyurethane epoxy resin material to the limitation of epoxy resin introduction amount; The properties of the resulting product are adjusted.

(2)本发明用聚氨酯预聚体、环氧树脂及哌嗪进行扩链聚合反应,其中哌嗪两端为仲胺基,在较低的温度下便能和异氰酸酯基、环氧基反应,因此,反应过程工艺简单、经济,并且它两个氨基为仲胺的特点,使合成出的聚氨酯-环氧树脂嵌段共聚水性树脂的胺值较低。(2) The present invention uses polyurethane prepolymer, epoxy resin and piperazine to carry out chain extension polymerization reaction, wherein both ends of piperazine are secondary amino groups, which can react with isocyanate groups and epoxy groups at lower temperatures, Therefore, the reaction process is simple and economical, and its two amino groups are secondary amines, so that the amine value of the synthesized polyurethane-epoxy resin block copolymerized water-based resin is low.

(3)本发明采用水溶性溶剂,水溶性溶剂能与水以任意比例混溶,因此,水在本发明中可做沉淀剂,从反应液中沉淀出前驱树脂,而产生的溶剂与水的混合液,经简单蒸馏脱水,便可回收利用。此方法免去了传统水性树脂制备过程中脱除溶剂的步骤,同时中和水化后的水性树脂,达到零VOC的目的。(3) The present invention adopts a water-soluble solvent, which can be miscible with water in any proportion. Therefore, water can be used as a precipitating agent in the present invention, and the precursor resin is precipitated from the reaction solution, and the resulting solvent is mixed with water. The mixed solution can be recycled after simple distillation and dehydration. This method eliminates the solvent removal step in the traditional water-based resin preparation process, and at the same time neutralizes the hydrated water-based resin to achieve the goal of zero VOC.

具体实施方式Detailed ways

以下结合具体实施例对本发明作进一步详细说明。The present invention will be described in further detail below in conjunction with specific examples.

实施例1 (对比例)Embodiment 1 (comparative example)

以配方参数Rt=1.10,H%=30w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.10, H%=30w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将25.39 g已除水的聚己内酯二元醇(分子量Mn=2000)和5.64 g异佛尔酮二异氰酸酯(IPDI)投入反应瓶中,反应温度为80℃,反应2h,制备得到聚氨酯预聚体31.03g;(1) Put 25.39 g of polycaprolactone diol (molecular weight Mn=2000) and 5.64 g of isophorone diisocyanate (IPDI) into the reaction bottle, the reaction temperature is 80 ℃, and react for 2 hours to prepare Obtain polyurethane prepolymer 31.03g;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为2︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 2:1;

(2)往步骤(1)所得聚氨酯预聚体中加入10.00 g环氧E-44、3.30 g哌嗪和40.21 gN,N-二甲基甲酰胺,搅拌均匀,升温至55℃,反应5 h;反应至环氧值为0,得混合物;(2) Add 10.00 g of epoxy E-44, 3.30 g of piperazine and 40.21 g of N,N-dimethylformamide to the polyurethane prepolymer obtained in step (1), stir evenly, heat up to 55°C, and react for 5 h ; Reaction until the epoxy value is 0, the mixture is obtained;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量2.9%的冰醋酸,搅拌5min,加入相当于前驱树脂质量2倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add glacial acetic acid equivalent to 2.9% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to twice the mass of the precursor resin, and stir for 30 minutes to emulsify, and you can get Polyurethane-epoxy resin block copolymerization water-based resin.

实施例2Example 2

以配方参数Rt=1.20,H%=30w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.20, H%=30w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将30.05 g已除水的聚己内酯二元醇(分子量Mn=2000)和6.69 g异佛尔酮二异氰酸酯(IPDI)投入反应瓶中,反应温度为80℃,反应2h,制备得到聚氨酯预聚体36.74g;(1) Put 30.05 g of polycaprolactone diol (molecular weight Mn=2000) and 6.69 g of isophorone diisocyanate (IPDI) into the reaction bottle, the reaction temperature is 80 ℃, and react for 2 hours to prepare Obtain polyurethane prepolymer 36.74g;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为2︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 2:1;

(2)往步骤(1)所得聚氨酯预聚体中加入11.59 g环氧E-44、4.16 g哌嗪和41.98 gN,N-二甲基甲酰胺,搅拌均匀,升温至55℃,反应5 h;反应至环氧值为0,得混合物;(2) Add 11.59 g of epoxy E-44, 4.16 g of piperazine and 41.98 g of N,N-dimethylformamide to the polyurethane prepolymer obtained in step (1), stir evenly, heat up to 55°C, and react for 5 h ; Reaction until the epoxy value is 0, the mixture is obtained;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量3.6%的冰醋酸,搅拌5min,加入相当于前驱树脂质量2倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add glacial acetic acid equivalent to 3.6% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to 2 times the mass of the precursor resin, and stir for 30 minutes to emulsify to obtain Polyurethane-epoxy resin block copolymerization water-based resin.

实施例3Example 3

以配方参数Rt=1.25,H%=30w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.25, H%=30w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将27.90 g已除水的聚己内酯二元醇(分子量Mn=2000)和6.21 g异佛尔酮二异氰酸酯(IPDI)投入反应瓶中,反应温度为80℃,反应2h,制备得到聚氨酯预聚体34.11g;(1) Put 27.90 g of polycaprolactone diol (molecular weight Mn=2000) and 6.21 g of isophorone diisocyanate (IPDI) into the reaction bottle, the reaction temperature is 80 ℃, and react for 2 hours to prepare Obtain polyurethane prepolymer 34.11g;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为2︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 2:1;

(2)往步骤(1)所得聚氨酯预聚体中加入10.63 g环氧E-44、3.99 g哌嗪和38.98 gN,N-二甲基甲酰胺,搅拌均匀,升温至55℃,反应5 h;反应至环氧值为0,得混合物;(2) Add 10.63 g of epoxy E-44, 3.99 g of piperazine and 38.98 g of N,N-dimethylformamide to the polyurethane prepolymer obtained in step (1), stir evenly, heat up to 55°C, and react for 5 h ; Reaction until the epoxy value is 0, the mixture is obtained;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量3.7%的冰醋酸,搅拌5min,加入相当于前驱树脂质量2倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add glacial acetic acid equivalent to 3.7% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to 2 times the mass of the precursor resin, and stir for 30 minutes to emulsify to obtain Polyurethane-epoxy resin block copolymerization water-based resin.

实施例4Example 4

以配方参数Rt=1.30,H%=30w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.30, H%=30w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将28.86 g已除水的聚己内酯二元醇(分子量Mn=2000)和6.42 g异佛尔酮二异氰酸酯(IPDI)投入反应瓶中,反应温度为80℃,反应2h,制备得到聚氨酯预聚体35.28g;(1) Put 28.86 g of polycaprolactone diol (molecular weight Mn=2000) and 6.42 g of isophorone diisocyanate (IPDI) into the reaction bottle, the reaction temperature is 80 ℃, and react for 2 hours to prepare Obtain polyurethane prepolymer 35.28g;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为2︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 2:1;

(2)往步骤(1)所得聚氨酯预聚体中加入10.86 g环氧E-44、4.26g哌嗪和40.32 gN,N-二甲基甲酰胺,搅拌均匀,搅拌升温至55℃,反应5 h;反应至环氧值为0,得混合物;(2) Add 10.86 g of epoxy E-44, 4.26 g of piperazine and 40.32 g of N,N-dimethylformamide to the polyurethane prepolymer obtained in step (1), stir evenly, heat up to 55°C, and react 5 h; react to epoxy value 0, get mixture;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量3.9%的冰醋酸,搅拌5min,加入相当于前驱树脂质量2倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add glacial acetic acid equivalent to 3.9% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to twice the mass of the precursor resin, and stir for 30 minutes to emulsify, and you can get Polyurethane-epoxy resin block copolymerization water-based resin.

实施例5Example 5

以配方参数Rt=1.30,H%=40w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.30, H%=40w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将30.44 g已除水的聚己内酯二元醇(分子量Mn=2000)和6.55 g异佛尔酮二异氰酸酯(IPDI)投入反应瓶中,反应温度为80℃,反应2h,制备得到聚氨酯预聚体36.99g;(1) Put 30.44 g of polycaprolactone diol (molecular weight Mn=2000) and 6.55 g of isophorone diisocyanate (IPDI) into the reaction bottle, the reaction temperature is 80 ℃, and react for 2 hours to prepare Obtain polyurethane prepolymer 36.99g;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为2︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 2:1;

(2)往步骤(1)所得聚氨酯预聚体中加入18.51 g环氧E-44、6.25 g哌嗪和49.41 gN,N-二甲基甲酰胺,搅拌均匀,升温至55℃,反应5 h;反应至环氧值为0,得混合物;(2) Add 18.51 g of epoxy E-44, 6.25 g of piperazine and 49.41 g of N,N-dimethylformamide to the polyurethane prepolymer obtained in step (1), stir evenly, heat up to 55°C, and react for 5 h ; Reaction until the epoxy value is 0, the mixture is obtained;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量5.0%的冰醋酸,搅拌5min,加入相当于前驱树脂质量2倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add glacial acetic acid equivalent to 5.0% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to 2 times the mass of the precursor resin, and stir for 30 minutes to emulsify to obtain Polyurethane-epoxy resin block copolymerization water-based resin.

实施例6Example 6

以配方参数Rt=1.30,H%=50w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.30, H%=50w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将25.00 g已除水的聚己内酯二元醇(分子量Mn=2000)和5.41 g异佛尔酮二异氰酸酯(IPDI)投入反应瓶中,反应温度为80℃,反应2h,制备得到聚氨酯预聚体30.41g;(1) Put 25.00 g of polycaprolactone diol (molecular weight Mn=2000) and 5.41 g of isophorone diisocyanate (IPDI) into the reaction bottle, the reaction temperature is 80 ℃, and react for 2 hours to prepare Obtain polyurethane prepolymer 30.41g;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为2︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 2:1;

(2)往步骤(1)所得聚氨酯预聚体中加入23.30 g环氧E-44、7.16 g哌嗪和48.70 gN,N-二甲基甲酰胺,搅拌均匀,升温至55℃,反应5 h;反应至环氧值为0,得混合物;(2) Add 23.30 g of epoxy E-44, 7.16 g of piperazine and 48.70 g of N,N-dimethylformamide to the polyurethane prepolymer obtained in step (1), stir evenly, heat up to 55°C, and react for 5 h ; Reaction until the epoxy value is 0, the mixture is obtained;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量6.4%的冰醋酸,搅拌5min,加入相当于前驱树脂质量2倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add glacial acetic acid equivalent to 6.4% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to 2 times the mass of the precursor resin, and stir for 30 minutes to emulsify to obtain Polyurethane-epoxy resin block copolymerization water-based resin.

实施例7Example 7

以配方参数Rt=1.25,H%=50w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.25, H%=50w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将13.40 g已除水的聚己内酯二元醇(分子量Mn=1000)和3.50g甲苯二异氰酸酯(TDI)投入反应瓶中,反应温度为60℃,反应2h,制备得到聚氨酯预聚体16.9g;(1) Put 13.40 g of dehydrated polycaprolactone diol (molecular weight Mn=1000) and 3.50 g of toluene diisocyanate (TDI) into the reaction bottle, the reaction temperature is 60 ℃, and react for 2 hours to prepare the polyurethane pre- Polymer 16.9g;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为1.5︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 1.5: 1;

(2)往步骤(1)所得聚氨酯预聚体中加入12.48 g环氧E-51、4.42g哌嗪和27.04 g四氢呋喃加入反应瓶中,搅拌均匀,升温至50℃,反应6 h;反应至环氧值为0,得混合物;(2) Add 12.48 g of epoxy E-51, 4.42 g of piperazine and 27.04 g of tetrahydrofuran to the polyurethane prepolymer obtained in step (1) into the reaction flask, stir evenly, raise the temperature to 50°C, and react for 6 h; The epoxy value is 0, and the mixture is obtained;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量10.0%的乳酸,搅拌5min,加入相当于前驱树脂质量3倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add lactic acid equivalent to 10.0% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to 3 times the mass of the precursor resin, and stir for 30 minutes to emulsify to obtain polyurethane -Epoxy resin block copolymerized water-based resin.

实施例8Example 8

以配方参数Rt=1.25,H%=50w%为例,聚氨酯-环氧树脂嵌段共聚水性树脂的制备方法如下:Taking formula parameters Rt=1.25, H%=50w% as an example, the preparation method of polyurethane-epoxy resin block copolymerized waterborne resin is as follows:

(1)将17.18g已除水的聚己二酸一缩二乙二醇酯(分子量Mn=2000)和2.60g六亚甲基二异氰酸酯(HDI)投入反应瓶中,反应温度为50℃,反应2h,制备得到聚氨酯预聚体11.61g;(1) Put 17.18g of polyethylene adipate (molecular weight Mn=2000) and 2.60g of hexamethylene diisocyanate (HDI) into the reaction flask, the reaction temperature is 50℃, After 2 hours of reaction, 11.61 g of polyurethane prepolymer was prepared;

所述低聚物二元醇和二异氰酸酯的比例,使得二异氰酸酯中的异氰酸酯基的物质的量与低聚物二元醇中[OH]的物质的量之比为1.8︰1;The ratio of the oligomer dibasic alcohol and diisocyanate makes the ratio of the amount of substance of the isocyanate group in the diisocyanate to the ratio of the amount of substance of [OH] in the oligomer dibasic alcohol be 1.8:1;

(2)往步骤(1)所得聚氨酯预聚体中加入17.02g环氧E-20、2.76g哌嗪和31.65gN-甲基吡咯烷酮,搅拌均匀,升温至45℃,反应7h;反应至环氧值为0,得混合物;(2) Add 17.02g of epoxy E-20, 2.76g of piperazine and 31.65g of N-methylpyrrolidone to the polyurethane prepolymer obtained in step (1), stir evenly, raise the temperature to 45°C, and react for 7 hours; A value of 0 results in a mixture;

(3)往步骤(2)所得混合物中加入与所加水溶性溶剂等质量的去离子水,搅拌均匀,再静置沉淀出聚合物,水洗聚合物,得到前驱树脂;(3) Add deionized water of the same quality as the added water-soluble solvent to the mixture obtained in step (2), stir evenly, then let stand to precipitate the polymer, wash the polymer with water, and obtain the precursor resin;

(4)将步骤(3)所得前驱树脂升温至45℃,加入相当于前驱树脂质量4.4%的丙酸,搅拌5min,加入相当于前驱树脂质量1.5倍的去离子水,搅拌30min乳化,即得到聚氨酯-环氧树脂嵌段共聚水性树脂。(4) Heat the precursor resin obtained in step (3) to 45°C, add propionic acid equivalent to 4.4% of the mass of the precursor resin, stir for 5 minutes, add deionized water equivalent to 1.5 times the mass of the precursor resin, stir for 30 minutes to emulsify, and then get Polyurethane-epoxy resin block copolymerization water-based resin.

各实施例所得聚氨酯-环氧树脂嵌段共聚水性树脂性能检测实施例:The performance detection embodiment of each embodiment gained polyurethane-epoxy resin block copolymerization waterborne resin:

检测前,将待检测聚氨酯-环氧树脂嵌段共聚水性树脂制备成固化物:将得到的聚氨酯-环氧树脂嵌段共聚水性树脂与BL3370 MPA按n(活泼氢):n(异氰酸酯基)=2复配,然后倒入聚四氟乙烯模具,待水挥发干,放入120℃烘箱中烘烤20min,即得到固化物样片。Before testing, the polyurethane-epoxy resin block copolymerization water-based resin to be tested is prepared into a cured product: the obtained polyurethane-epoxy resin block copolymerization water-based resin and BL3370 MPA are pressed according to n (active hydrogen): n (isocyanate group) = 2 Compounding, then pour into a polytetrafluoroethylene mold, wait for the water to evaporate and dry, put it in a 120°C oven and bake for 20 minutes, and then obtain a cured product sample.

各实施例所得聚氨酯-环氧树脂嵌段共聚树脂在阴极电泳中的应用,可以采用以下方法:The application of each embodiment gained polyurethane-epoxy resin block copolymer resin in cathodic electrophoresis can adopt the following methods:

先取所制备的聚氨酯-环氧树脂嵌段共聚树脂,将其与封闭型异氰酸酯按一定比例加入到容器中,用分散机搅拌至均相,搅拌速度为600r/min,然后加入适量的有机酸,继续搅拌5min,然后往容器中加入去离子水,搅拌30min后,将乳液固含量调整至20w%,即得到分散均匀的电泳乳液;以马口铁或其他金属板作阴极,在电泳电压40-120V下电泳30-150s;结束后,取出金属板,用去离子水冲洗沉积层表面,在120℃下烘烤30min,最终得到涂膜平整光滑的样件。First take the prepared polyurethane-epoxy resin block copolymer resin, add it and blocked isocyanate into the container in a certain proportion, stir until homogeneous with a disperser, the stirring speed is 600r/min, and then add an appropriate amount of organic acid, Continue to stir for 5 minutes, then add deionized water into the container, after stirring for 30 minutes, adjust the solid content of the emulsion to 20w%, and then obtain a uniformly dispersed electrophoretic emulsion; use tinplate or other metal plates as cathodes, and use electrophoresis voltage 40-120V Electrophoresis for 30-150s; after the end, take out the metal plate, rinse the surface of the deposited layer with deionized water, bake at 120°C for 30min, and finally obtain a sample with a flat and smooth coating film.

实验结果与表征Experimental Results and Characterization

通过上述实施例1~实施例8的研究,探索了配方参数对树脂结构参数、水性树脂性能、水性树脂固化物性能、树脂阴极电泳液及漆膜性能的影响。其表征结果如下所述。Through the research of Examples 1 to 8 above, the effects of formula parameters on resin structure parameters, water-based resin performance, water-based resin cured product performance, resin cathodic electrophoretic fluid and paint film performance were explored. The characterization results are as follows.

(一)配方参数对树脂结构参数的影响(1) Influence of formula parameters on resin structure parameters

探究了Rt对合成树脂分子量的影响。实验结果如表1所示。The effect of Rt on the molecular weight of the synthetic resin was explored. The experimental results are shown in Table 1.

由表1可知,Rt增加,合成树脂的分子量减小,分子量分布(D)总体变大。因为Rt越大,氨基物质过量越多,形成端氨基大分子数量越多,故树脂分子量越小;当合成树脂的分子量小,即聚合度小时,聚合度相邻的两个分子间的分子量的相对差距变大,故分子量分布变宽。It can be seen from Table 1 that as Rt increases, the molecular weight of the synthetic resin decreases, and the molecular weight distribution (D) increases overall. Because the larger the Rt, the more excess amino substances, the more the number of amino-terminated macromolecules formed, the smaller the molecular weight of the resin; The relative gap becomes larger, so the molecular weight distribution becomes wider.

(二)配方参数对水性树脂性能的影响(2) The influence of formula parameters on the performance of water-based resin

探究了配方参数对水性树脂性能的影响。实验结果如表2。The influence of formulation parameters on the properties of waterborne resins was explored. The experimental results are shown in Table 2.

由表2可知,当H%不变,Rt为1.10时,合成树脂不能被水化;当Rt≥1.20时,乳液的粒径随Rt的增加而减小,这主要是因为,合成树脂的分子量减小,而胺值增加,故在相同中和度的情况下,被离子化的胺基增加,树脂亲水性增加。It can be seen from Table 2 that when H% is constant and Rt is 1.10, the synthetic resin cannot be hydrated; when Rt≥1.20, the particle size of the emulsion decreases with the increase of Rt, which is mainly because the molecular weight of the synthetic resin Decrease, while the amine value increases, so under the same degree of neutralization, the number of ionized amine groups increases, and the hydrophilicity of the resin increases.

当Rt不变时,乳液的粒径随H%的增加而减小,这主要是因为H%增加,合成树脂胺值增加,在相同中和度的情况下,树脂被离子化的胺基增加,树脂亲水性增加。When Rt is constant, the particle size of the emulsion decreases with the increase of H%, which is mainly because the amine value of the synthetic resin increases with the increase of H%, and under the same degree of neutralization, the ionized amine groups of the resin increase , the hydrophilicity of the resin increases.

(三)配方参数对固化物性能的影响(3) The influence of formula parameters on the properties of cured products

探究了配方参数对合成树脂固化物的力学性能的影响。实验结果如表3。The influence of formulation parameters on the mechanical properties of synthetic resin cured products was explored. The experimental results are shown in Table 3.

从表3可知,当H%不变Rt变大时,拉伸强度变小,而断裂伸长率变大,主要是因为一方面Rt大,合成树脂的分子量小,即分子链短,分子链之间的物理缠结点少;另一方面Rt大,树脂的活泼氢量少,导致树脂的化学交联点少。It can be seen from Table 3 that when H% remains constant and Rt increases, the tensile strength decreases and the elongation at break increases, mainly because on the one hand the Rt is large and the molecular weight of the synthetic resin is small, that is, the molecular chain is short and the molecular chain There are few physical entanglement points between them; on the other hand, the Rt is large, and the active hydrogen content of the resin is small, resulting in few chemical crosslinking points of the resin.

当Rt不变H%变大时,拉伸强度增大,断裂伸长率减小,主要是因为一方面H%增大,改性树脂的刚性结构增多,增加了固化物内聚力;另一方面H%增大,树脂的活泼氢量增加,树脂的化学交联点增多。When Rt remains unchanged and H% increases, the tensile strength increases and the elongation at break decreases, mainly because on the one hand, H% increases, the rigid structure of the modified resin increases, and the cohesion of the cured product increases; on the other hand H% increases, the active hydrogen content of the resin increases, and the chemical crosslinking points of the resin increase.

(四)配方参数对树脂阴极电泳液性能的影响(4) Influence of formulation parameters on the performance of resin cathodic electrophoretic fluid

探究了配方参数对树脂阴极电泳液性能的影响。实验结果如表4。The influence of formulation parameters on the performance of resin cathodic electrophoretic fluid was explored. The experimental results are shown in Table 4.

由表4可知,当H%不变,Rt为1.20时,合成树脂制备得到的阴极电泳液为乳白色浑浊液体,且机械稳定性和存储稳定性都不达标,这主要是因为合成树脂分子量大,且可被离子化的胺基较少,因此,其亲水性较差,包裹封闭型固化剂后,乳液的分散稳定性较差(此种情况下的树脂只能作为水性涂料);当Rt≥1.25时,电泳液的电导率和pH值随着Rt 的增加而增加,这主要是因为合成树脂的分子量减小,而胺值增加,故在相同中和度的情况下,被离子化的胺基增加,且胺基既是成盐基团又是碱性基团,因此,Rt增加,电泳液的电导率和pH都升高。It can be seen from Table 4 that when H% is constant and Rt is 1.20, the cathodic electrophoresis liquid prepared by synthetic resin is a milky white turbid liquid, and the mechanical stability and storage stability are not up to standard. This is mainly because the synthetic resin has a large molecular weight. And there are fewer amine groups that can be ionized, so its hydrophilicity is poor. After wrapping the closed curing agent, the dispersion stability of the emulsion is poor (the resin in this case can only be used as a water-based coating); when Rt When ≥1.25, the conductivity and pH value of the electrophoretic solution increase with the increase of Rt, which is mainly because the molecular weight of the synthetic resin decreases and the amine value increases, so under the same degree of neutralization, the ionized The amine group increases, and the amine group is both a salt-forming group and a basic group. Therefore, the Rt increases, and the conductivity and pH of the electrophoretic solution increase.

当Rt不变,H%含量增加时,电泳液的电导率和pH值随着H%的增加而增加,这主要是因为H%增加,合成树脂引入的胺基基团数增加,即胺值变大,因此,在相同中和度的情况下,被离子化的胺基增加,且胺基既是可被离子化的基团又是碱性基团,故H%增加,电泳液的电导率和pH都升高。When the Rt is constant and the H% content increases, the conductivity and pH of the electrophoretic solution increase with the increase of H%, which is mainly because the increase of H% increases the number of amine groups introduced by the synthetic resin, that is, the amine value Therefore, under the same degree of neutralization, the ionized amine group increases, and the amine group is both an ionizable group and a basic group, so H% increases, and the conductivity of the electrophoretic solution and pH increase.

(五)配方参数对电泳漆膜性能的影响(5) The influence of formula parameters on the performance of electrophoretic paint film

探究了配方参数对电泳漆膜性能的影响。实验结果如表5。The influence of formula parameters on the performance of electrophoretic paint film was explored. The experimental results are shown in Table 5.

由表5知,在相同的电泳条件下,在H%不变Rt增加时,漆膜的硬度减小,厚度以及光泽度增加,耐水性和耐酸碱性降低,且在Rt = 1.25时,漆膜耐碱性比耐酸性强很多。这是主要是因为,一方面Rt增加,改性树脂的分子量小,即分子链短,分子链之间的物理缠结点少,并且树脂的活泼氢量少,导致树脂的化学交联点少,因此漆膜硬度、耐水性以及耐酸碱性减小;一方面Rt增加,合成树脂的胺值增大,胺基既是成盐基团又是亲水性基团,因此,胺值增加使合成树脂阴极电泳液的导电率增加的同时,降低了合成树脂的耐水性,故在相同电泳条件下漆膜的厚度增加,漆膜的耐水性降低。另一方面带正电胶粒在阴极附近被OH-中和析出,得到的涂层烘烤后固化成漆膜,因此,在酸性条件下,漆膜中的胺基被离子化,易使漆膜出现反溶现象,然而在碱性条件中则不会出现此现象,故在Rt = 1.25时,漆膜的耐碱性比耐酸性强很多。It is known from Table 5 that under the same electrophoresis conditions, when H% is constant and Rt increases, the hardness of the paint film decreases, the thickness and gloss increase, and the water resistance and acid and alkali resistance decrease, and when Rt = 1.25, The paint film is much more resistant to alkali than to acid. This is mainly because, on the one hand, the Rt increases, the molecular weight of the modified resin is small, that is, the molecular chain is short, the physical entanglement points between the molecular chains are few, and the active hydrogen content of the resin is small, resulting in few chemical crosslinking points of the resin. , so the paint film hardness, water resistance, and acid and alkali resistance decrease; on the one hand, the increase in Rt increases the amine value of the synthetic resin, and the amine group is both a salt-forming group and a hydrophilic group. Therefore, the increase in the amine value makes While the conductivity of the synthetic resin cathodic electrophoretic fluid increases, the water resistance of the synthetic resin decreases, so the thickness of the paint film increases under the same electrophoresis conditions, and the water resistance of the paint film decreases. On the other hand, the positively charged colloidal particles are neutralized and precipitated by OH- near the cathode, and the obtained coating is cured into a paint film after baking. Therefore, under acidic conditions, the amine groups in the paint film are ionized, which is easy to make the paint However, this phenomenon does not occur in alkaline conditions, so when Rt = 1.25, the alkali resistance of the paint film is much stronger than the acid resistance.

由表知,在相同的电泳条件下,Rt不变H%增加,漆膜的厚度、硬度以及耐碱性增加,光泽度及耐水性减小,且总体上耐碱性比耐酸性强,这是主要是因为一方面H%增加,合成树脂的刚性结构增多,增加了固化物内聚力,并且树脂的活泼氢量增加,树脂的化学交联点增多,因此,H%升高,漆膜硬度以及耐碱性增加;一方面,H%增加,合成树脂的胺值增大,胺基既是成盐基团又是亲水性基团,因此,阴极电泳液的导电率增加的同时,降低了合成树脂的耐水性,而在相同电泳条件下,带电胶粒迁移的速度增加,即电沉积的速度增加,但电沉积速度超过一定速度时,容易使漆膜变粗糙甚至出现堆积现象,因此,H%升高,漆膜厚度变大,光泽度及耐水性降低。另一方面带正电胶粒在阴极附近被OH-中和析出,得到的涂层烘烤后固化成漆膜,因此,在酸性条件下,漆膜中的胺基被离子化,易使漆膜出现反溶现象,然而在碱性条件中则不会出现此现象,故总体上漆膜的耐碱性比耐酸性强。It is known from the table that under the same electrophoresis conditions, Rt remains unchanged and H% increases, the thickness, hardness and alkali resistance of the paint film increase, the gloss and water resistance decrease, and the alkali resistance is generally stronger than the acid resistance. The main reason is that on the one hand, the increase of H% increases the rigid structure of the synthetic resin, increases the cohesion of the cured product, and the active hydrogen content of the resin increases, and the chemical crosslinking points of the resin increase. Therefore, the increase of H% increases the hardness of the paint film and Alkali resistance increases; on the one hand, as H% increases, the amine value of the synthetic resin increases, and the amine group is both a salt-forming group and a hydrophilic group. Therefore, while the conductivity of the cathodic electrophoretic solution increases, the synthetic The water resistance of the resin, and under the same electrophoresis conditions, the migration speed of charged colloidal particles increases, that is, the speed of electrodeposition increases, but when the speed of electrodeposition exceeds a certain speed, it is easy to make the paint film rough and even pile up. Therefore, H % increases, the thickness of the paint film becomes larger, and the gloss and water resistance decrease. On the other hand, the positively charged colloidal particles are neutralized and precipitated by OH- near the cathode, and the obtained coating is cured into a paint film after baking. Therefore, under acidic conditions, the amine groups in the paint film are ionized, which is easy to make the paint The anti-dissolution phenomenon of the film appears, but this phenomenon does not appear in alkaline conditions, so the alkali resistance of the paint film is stronger than the acid resistance in general.

附检测方法:Attached detection method:

1、水性树脂及其制备的电泳液性能测试1. Performance test of water-based resin and its prepared electrophoretic fluid

(1)环氧值的测定(1) Determination of epoxy value

称取0.5000-1.5000 g树脂,置于150 ml的锥形瓶中,加入20.0 ml盐酸-丙酮溶液(浓盐酸l ml,溶于40 ml丙酮中,现用现配),塞紧瓶塞,摇匀,使试样完全溶解。置于阴凉处1小时,滴加2-3滴甲基红指示剂,然后用0.2 mol/LNa0H标准溶液滴定,溶液颜色由红变黄时即为终点,同样做空白实验,计算方法如下:Weigh 0.5000-1.5000 g of resin, place it in a 150 ml Erlenmeyer flask, add 20.0 ml of hydrochloric acid-acetone solution (1 ml of concentrated hydrochloric acid, dissolved in 40 ml of acetone, ready-to-use), stopper the bottle tightly, shake Mix well to dissolve the sample completely. Put it in a cool place for 1 hour, add 2-3 drops of methyl red indicator dropwise, and then titrate with 0.2 mol/L NaOH standard solution. When the color of the solution changes from red to yellow, it is the end point. Do the same blank experiment, and the calculation method is as follows:

式中:E----环氧值(mol/100g);In the formula: E ---- epoxy value (mol/100g);

V0----空白所消耗的Na0H溶液体积(ml);V 0 ---- the volume of NaOH solution consumed by the blank (ml);

V1----样品所消耗的NaOH溶液体积(ml);V 1 ---- the volume of NaOH solution consumed by the sample (ml);

W----样品的质量(g);W ---- the quality of the sample (g);

NNaOH----NaOH的溶液的浓度(mol/L);N NaOH - the concentration of NaOH solution (mol/L);

(1)乳液外观:目测观察制得的乳液状态。例:颜色、透明度、有无凝聚等;(1) Emulsion Appearance: Visually observe the state of the prepared emulsion. Example: color, transparency, presence or absence of condensation, etc.;

(2)乳液固含量:参照《GB/T 1725-2007 色漆、清漆和塑胶不挥发物含量的测定》;(2) Emulsion solid content: refer to "GB/T 1725-2007 Determination of non-volatile content of paints, varnishes and plastics";

(3)乳液机械稳定性:对于乳液的机械稳定性尚无相关测试标准,参考已有的实验方法暂定如表所示。(3) Mechanical stability of the emulsion: There is no relevant test standard for the mechanical stability of the emulsion, and it is tentatively shown in the table with reference to the existing experimental methods.

机械稳定性级别及分级方法 级别 分级方法 1级 1500 r/min×20 min下不分相 2级 2000 r/min×20 min下不分相 3级 2500 r/min×20 min下不分相 4级 3000 r/min×20 min下不分相 5级 3500 r/min×20 min下不分相 6级 4000 r/min×20 min下不分相 Mechanical stability level and classification method level Grading method Level 1 No phase separation at 1500 r/min×20 min level 2 No phase separation at 2000 r/min×20 min Level 3 No phase separation at 2500 r/min×20 min level 4 No phase separation at 3000 r/min×20 min Level 5 No phase separation at 3500 r/min×20 min Level 6 No phase separation at 4000 r/min×20 min

其中,级别越高,表示电泳涂料乳液的稳定性越好。一般在 3000 r/min 下离心 20min 不分相就可以认为常温静置 6 个月乳液不分相。Among them, the higher the level, the better the stability of the electrophoretic coating emulsion. Generally, if there is no phase separation after centrifugation at 3000 r/min for 20 minutes, it can be considered that the emulsion has no phase separation after standing at room temperature for 6 months.

(4)电泳液pH测定:采用PHS-3C型pH计测定;(4) pH measurement of electrophoresis solution: use PHS-3C pH meter to measure;

(5)电泳液电导率测定:参照HG/T3335-1997(1985)《电泳漆电导率测定方法》;(5) Determination of the conductivity of the electrophoretic solution: refer to HG/T3335-1997 (1985) "Methods for the determination of the conductivity of electrophoretic paint";

(6)乳液粒径测定:采用英国马尔文公司Zetasizer Nano ZS型粒度分布仪测定乳液的粒径及分布。(6) Determination of particle size of the emulsion: The particle size and distribution of the emulsion were measured with a Zetasizer Nano ZS particle size distribution analyzer from Malvern, UK.

、固化物性能测试, Cured product performance test

参考ASTM D2707-1985,将固化物裁剪成标准样条,在室温下用拉伸测试仪以90mm/min的拉伸速度进行拉伸试验,测试固化物的拉伸强度以及断裂伸长率。Referring to ASTM D2707-1985, the cured product was cut into a standard sample, and a tensile test was performed at room temperature with a tensile tester at a tensile speed of 90 mm/min to test the tensile strength and elongation at break of the cured product.

、涂层性能测试, coating performance test

(1)铅笔硬度:参照《GB/T 6739-2006/ISO 15184:1998 色漆和清漆铅笔法测定漆膜硬度》;(1) Pencil hardness: refer to "GB/T 6739-2006/ISO 15184:1998 Paint and Varnish Pencil Method for Determination of Paint Film Hardness";

(2)附着力:参照《GB/T 9286-1998/ISO 2409:1992色漆和清漆漆膜的划格试验》;(2) Adhesion: refer to "GB/T 9286-1998/ISO 2409:1992 Cross-cut test of paint and varnish film";

(3)柔韧性:参照《GB/T 1731-1993漆膜柔韧性测定法》;(3) Flexibility: Refer to "GB/T 1731-1993 Determination of Paint Film Flexibility";

(4)漆膜膜厚的测定:采用DR-330涂层测厚仪测定;(4) Determination of paint film thickness: measured by DR-330 coating thickness gauge;

(5)漆膜光泽度的测定:参照《GB/T9754-2007色漆和清漆、不含金属颜料的色漆漆膜之20°、60°和85°镜面光泽的测定》。(5) Determination of paint film gloss: refer to "Determination of 20°, 60° and 85° specular gloss of paint films of paints and varnishes and paint films without metallic pigments" GB/T9754-2007.

Claims (10)

1. a kind of preparation method of polyurethane-epoxy resin block copolymerization water-base resin, which comprises the following steps:
(1) by oligomer dihydric alcohol and diisocyanate investment reaction flask, reaction temperature is 50 DEG C ~ 80 DEG C, reacts 1 ~ 3h, system It is standby to obtain base polyurethane prepolymer for use as;
(2) epoxy resin, piperazine and water-soluble solvent is added into step (1) gained base polyurethane prepolymer for use as, stirs evenly, heats up To 30 DEG C ~ 70 DEG C, 3 ~ 8 h are reacted, reaction to epoxide number is 0, obtains mixture;
(3) deionized water with quality such as added water-soluble solvents is added into step (2) gained mixture, stirs evenly, then Polymer is staticly settled out, polymer is washed, obtains precursor resin;
(4) precursor resin obtained by step (3) is warming up to 40-55 DEG C, addition is equivalent to having for precursor resin quality 1.2 ~ 16.0% Machine acid, stirs 3-10min, and the deionized water for being equivalent to 1-3 times of precursor resin quality is added, and it is poly- to get arriving to stir 20-35min Urethane-epoxy resin block copolymerization water-base resin.
2. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1, feature exist In, in step (1), the ratio of the oligomer dihydric alcohol and diisocyanate, so that the isocyanate group in diisocyanate Substance amount and the ratio between the amount of substance of [OH] in oligomer dihydric alcohol be 1.5-2 ︰ 1.
3. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature Be, in step (2), the additional amount of the water-soluble solvent, be base polyurethane prepolymer for use as, epoxy resin, piperazine gross mass 60- 100%;
The proportion of epoxy resin and piperazine is controlled with chain extension parameter Rt and hard segment content H%;
Control chain extension parameter Rt=1.2 ~ 1.6, Rt={ n (amino)/[n (epoxy group)+n (isocyanate group)] }, n expression thing The amount of matter;Amino is the secondary amine in piperazine, and epoxy group is the epoxy group in epoxy resin, and isocyanate group is base polyurethane prepolymer for use as In isocyanate group;
Controlling hard segment content H% is 10 ~ 60%;H%={ [m (epoxy resin)+m (piperazine)]/[m (epoxy resin)+m (piperazine) + m (base polyurethane prepolymer for use as)] }, m indicates the quality of substance;Hard segment content H% is hard segment content, adjustable synthetic resin Flexibility.
4. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature It is, in step (1), the oligomer dihydric alcohol is polycaprolactone diols, polyadipate diglycol ester, poly- tetrahydro At least one of furans dihydric alcohol.
5. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature It is, in step (1), the oligomer dihydric alcohol molecular weight is 400-4000.
6. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature It is, in step (1), the diisocyanate is toluene di-isocyanate(TDI), isophorone diisocyanate, diphenyl methane two At least one of isocyanates, hexamethylene diisocyanate.
7. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature It is, in step (2), the epoxy resin is at least one of epoxy E-51, epoxy E-44, epoxy E-20, epoxy E-12.
8. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature It is, in step (2), the water-soluble solvent is n,N-Dimethylformamide, tetrahydrofuran, acetone, N-Methyl pyrrolidone One or both of.
9. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature It is, in step (2), control reaction is 45-60 DEG C of temperature;The control reaction time is 4-6h.
10. the preparation method of polyurethane-epoxy resin block copolymerization water-base resin according to claim 1 or 2, feature It is, in step (4), the organic acid is at least one of glacial acetic acid, lactic acid, formic acid, propionic acid, oxalic acid.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111484627A (en) * 2020-04-26 2020-08-04 赵汉波 Functional boron nitride in-situ modified epoxy resin insulating material and preparation method thereof
CN112143470A (en) * 2019-06-28 2020-12-29 中国石油化工股份有限公司 Plugging material, preparation method thereof and plugging agent
CN114230749A (en) * 2021-11-29 2022-03-25 西安交通大学 Epoxy resin cured material capable of being quickly self-repaired, preparation method and application
CN114773610A (en) * 2022-05-24 2022-07-22 台州市黄岩区武汉理工高性能复合材料技术研究院 Preparation method of polyurethane toughened epoxy resin

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1280156A (en) * 2000-07-11 2001-01-17 湖北省化学研究所 Anisotyopic conductive adhesive and its preparing method
US6878794B1 (en) * 1998-06-03 2005-04-12 Tennant Company Urethane resins
CN101717488A (en) * 2009-12-03 2010-06-02 上海维凯化学品有限公司 Epoxy resin modified water-based polyurethane emulsion and preparation method thereof
WO2010074732A1 (en) * 2008-12-22 2010-07-01 The Sherwin-Williams Company Photocurable interpenetrating polymer networks
CN101831045A (en) * 2010-04-30 2010-09-15 北京化工大学 High-performance rigid polyurethane foam material containing epoxide group
CN106811062A (en) * 2015-11-27 2017-06-09 重庆市共赢包装制品有限公司 The preparation method of epoxy modified polyurethane package coating

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6878794B1 (en) * 1998-06-03 2005-04-12 Tennant Company Urethane resins
CN1280156A (en) * 2000-07-11 2001-01-17 湖北省化学研究所 Anisotyopic conductive adhesive and its preparing method
WO2010074732A1 (en) * 2008-12-22 2010-07-01 The Sherwin-Williams Company Photocurable interpenetrating polymer networks
CN101717488A (en) * 2009-12-03 2010-06-02 上海维凯化学品有限公司 Epoxy resin modified water-based polyurethane emulsion and preparation method thereof
CN101831045A (en) * 2010-04-30 2010-09-15 北京化工大学 High-performance rigid polyurethane foam material containing epoxide group
CN106811062A (en) * 2015-11-27 2017-06-09 重庆市共赢包装制品有限公司 The preparation method of epoxy modified polyurethane package coating

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112143470A (en) * 2019-06-28 2020-12-29 中国石油化工股份有限公司 Plugging material, preparation method thereof and plugging agent
CN111484627A (en) * 2020-04-26 2020-08-04 赵汉波 Functional boron nitride in-situ modified epoxy resin insulating material and preparation method thereof
CN114230749A (en) * 2021-11-29 2022-03-25 西安交通大学 Epoxy resin cured material capable of being quickly self-repaired, preparation method and application
CN114230749B (en) * 2021-11-29 2023-03-17 西安交通大学 Epoxy resin cured material capable of being quickly self-repaired, preparation method and application
CN114773610A (en) * 2022-05-24 2022-07-22 台州市黄岩区武汉理工高性能复合材料技术研究院 Preparation method of polyurethane toughened epoxy resin

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