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CN108178818A - Reversed core-shell emulsion of NMA modified polyvinyl acetate bases and preparation method thereof - Google Patents

Reversed core-shell emulsion of NMA modified polyvinyl acetate bases and preparation method thereof Download PDF

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CN108178818A
CN108178818A CN201711467929.5A CN201711467929A CN108178818A CN 108178818 A CN108178818 A CN 108178818A CN 201711467929 A CN201711467929 A CN 201711467929A CN 108178818 A CN108178818 A CN 108178818A
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nma
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emulsion
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modified polyvinyl
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CN108178818B (en
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李志国
孙嘉星
张霄
加朝
顾继友
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Northeast Forestry University
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Abstract

本发明属于乳液胶黏剂制备领域,具体涉及一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液及其制备方法,所述乳液主要由醋酸乙烯酯、苯乙烯和功能单体NMA制成,乳液中的复合乳胶粒呈草莓型核壳结构,以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳,在复合乳胶粒表面添加有功能单体NMA。本发明乳液胶黏剂在保持良好胶接性能和反向结构复合乳胶粒优良耐水热性能的同时,利用NMA的自交联属性有效地提高了乳液胶黏剂的胶接湿强度,同时可以提高乳液胶黏剂的初粘性,又由于NMA为亲水性基团,可以极大改善乳液胶黏剂对被胶接对象的润湿性。本发明提供的乳液胶黏剂无毒无害、无污染,可广泛应用于纸张包装、家具制造、室内装修、地板铺设和胶合木材等领域。

The invention belongs to the field of emulsion adhesive preparation, and specifically relates to an NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion and a preparation method thereof. The emulsion is mainly made of vinyl acetate, styrene and functional monomer NMA The composite latex particles in the emulsion have a strawberry-shaped core-shell structure, with polyvinyl acetate as the core and small polystyrene particles as the shell, and functional monomer NMA is added on the surface of the composite latex particles. The emulsion adhesive of the present invention can effectively improve the bonding wet strength of the emulsion adhesive by utilizing the self-crosslinking properties of NMA while maintaining good bonding performance and the excellent hydrothermal resistance of the reverse structure composite latex particles, and at the same time can improve The initial tack of the emulsion adhesive, and because NMA is a hydrophilic group, can greatly improve the wettability of the emulsion adhesive to the objects to be bonded. The emulsion adhesive provided by the invention is non-toxic, harmless and pollution-free, and can be widely used in the fields of paper packaging, furniture manufacturing, interior decoration, floor laying, gluing wood and the like.

Description

NMA改性聚醋酸乙烯酯基反向核壳结构乳液及其制备方法NMA modified polyvinyl acetate based reverse core-shell structure emulsion and preparation method thereof

技术领域technical field

本发明属于乳液胶黏剂制备领域,具体涉及一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液及其制备方法。The invention belongs to the field of emulsion adhesive preparation, and in particular relates to an NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion and a preparation method thereof.

背景技术Background technique

构建聚醋酸乙烯酯(PVAc)基核壳结构乳液可以在保持原乳液胶膜成膜性能与粘接性能的同时,通过引入苯乙烯(St)等较难进行传统共聚而性能优异的改性单体,提高乳液的耐水性、耐热性和抗蠕变性能。构建以聚醋酸乙烯酯为核、聚苯乙烯为壳的反向核壳结构化乳液,虽然可以提高乳液的压缩剪切强度、耐水性、冻融稳定性,但苯乙烯为刚性单体,单体中没有活性官能基团,复合到聚醋酸乙烯酯胶粒表层后,虽然可以提高乳胶膜强度以及耐水性,但是乳液的胶接性能将受到影响。此外,湿热条件对乳液胶层的破坏极大,影响胶层的胶接湿强度,这大大限制了乳液胶黏剂的实际应用。The construction of polyvinyl acetate (PVAc)-based core-shell structure emulsion can maintain the film-forming and adhesive properties of the original emulsion film, and at the same time introduce styrene (St) and other modified monomers that are difficult to carry out traditional copolymerization and have excellent performance. Body, improve the water resistance, heat resistance and creep resistance of the emulsion. Constructing a reverse core-shell structured emulsion with polyvinyl acetate as the core and polystyrene as the shell can improve the compressive shear strength, water resistance, and freeze-thaw stability of the emulsion, but styrene is a rigid monomer. There are no active functional groups in the body. After compounding to the surface layer of polyvinyl acetate particles, although the strength and water resistance of the latex film can be improved, the bonding performance of the emulsion will be affected. In addition, hot and humid conditions can greatly damage the emulsion adhesive layer, which affects the bonding wet strength of the adhesive layer, which greatly limits the practical application of emulsion adhesives.

发明内容Contents of the invention

为解决上述现有技术的不足,本发明提供了一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液及其制备方法。In order to solve the above-mentioned deficiencies in the prior art, the present invention provides an NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion and a preparation method thereof.

本发明的技术方案:Technical scheme of the present invention:

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液,主要由醋酸乙烯酯、苯乙烯和功能单体NMA制成,所述乳液中的复合乳胶粒呈草莓型核壳结构,以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳,在所述复合乳胶粒表面添加有功能单体NMA。An NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion, mainly made of vinyl acetate, styrene and functional monomer NMA, the composite latex particles in the emulsion have a strawberry-shaped core-shell structure, with poly Vinyl acetate is the core, small polystyrene particles are the shell, and functional monomer NMA is added on the surface of the composite latex particles.

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液的制备方法步骤如下:A kind of preparation method step of NMA modified polyvinyl acetate base reverse core-shell structure emulsion is as follows:

步骤一、将pH缓冲剂和复合乳化剂加入一定质量的去离子水中,升温至60℃,搅拌一定时间后加入占醋酸乙烯酯单体总重量10~20%的醋酸乙烯酯单体,搅拌乳化一定时间后,加入占引发剂总重量30~50%的引发剂水溶液,升温至65℃继续反应,待出现蓝光后继续升温至80℃,反应一定时间后制得核种子乳液;Step 1. Add the pH buffer and compound emulsifier into deionized water of a certain quality, raise the temperature to 60°C, stir for a certain period of time, add vinyl acetate monomer accounting for 10-20% of the total weight of vinyl acetate monomer, stir and emulsify After a certain period of time, add an aqueous initiator solution accounting for 30-50% of the total weight of the initiator, heat up to 65°C to continue the reaction, and continue to heat up to 80°C after the blue light appears, and react for a certain period of time to prepare a nuclear seed emulsion;

步骤二、将步骤一制得的核种子乳液维持反应温度为80℃,逐滴滴加剩余的醋酸乙烯酯单体和丙烯酸丁酯单体的混合物到上述核种子乳液中,此滴加过程中,等量分批补加剩余的引发剂;待核单体混合物滴加完毕后,将接枝单体滴加入反应体系中,待接枝单体滴加完毕后马上开始滴加苯乙烯壳单体,待苯乙烯壳单体滴加完毕后,升温至85℃,保温一定时间后将乳液降温至60℃,此时开始滴加一定比例的NMA功能单体,NMA功能单体滴加完毕后升温至80℃,保温一定时间后将反应体系自然冷却至室温,过滤,得到NMA改性聚醋酸乙烯酯基反向核壳结构乳液。Step 2. Maintain the reaction temperature of the nuclear seed emulsion prepared in step 1 at 80°C, and dropwise add the mixture of the remaining vinyl acetate monomer and butyl acrylate monomer to the above-mentioned nuclear seed emulsion. , add the remaining initiator in batches in equal amounts; after the dropwise addition of the core monomer mixture is completed, the grafted monomer is added dropwise into the reaction system, and the styrene shell monomer is added dropwise immediately after the addition of the grafted monomer is completed. After the styrene shell monomer is added dropwise, the temperature is raised to 85°C, and after holding for a certain period of time, the temperature of the emulsion is lowered to 60°C. At this time, a certain proportion of NMA functional monomer is added dropwise. The temperature was raised to 80°C, and after a certain period of time, the reaction system was naturally cooled to room temperature and filtered to obtain an NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion.

进一步的,按反应的醋酸乙烯酯单体和苯乙烯单体总量为基准计,所用各原料的重量配比如下:Further, based on the total amount of vinyl acetate monomer and styrene monomer reacted, the weight ratio of each raw material used is as follows:

进一步的,所述pH缓冲剂为NaHCO3;所述复合乳化剂由乳化剂PCA507和乳化剂PCA078组成,其中PCA507与PCA078的重量比为(1~2):(1~2);所述引发剂为过硫酸铵,引发剂水溶液是将过硫酸铵用占去离子水总重量的10~15%的去离子水溶解配制而成;所述接枝单体为马来酸酐,马来酸酐单体是将马来酸酐用占去离子水总重量的5~10%的去离子水溶解配制而成。Further, the pH buffering agent is NaHCO3; the composite emulsifier is composed of emulsifier PCA507 and emulsifier PCA078, wherein the weight ratio of PCA507 and PCA078 is (1~2):(1~2); the initiator It is ammonium persulfate, and the initiator aqueous solution is prepared by dissolving ammonium persulfate in deionized water accounting for 10% to 15% of the total weight of deionized water; the graft monomer is maleic anhydride, maleic anhydride monomer It is prepared by dissolving maleic anhydride in deionized water accounting for 5-10% of the total weight of deionized water.

进一步的,步骤一所述将pH缓冲剂和复合乳化剂加入去离子水中升温至60℃后的搅拌时间为30min;所述加入醋酸乙烯酯单体后搅拌乳化的时间为30min;所述出现蓝光后继续升温至80℃进行反应的时间为30min。Further, the stirring time after adding the pH buffer and the composite emulsifier into the deionized water and raising the temperature to 60°C in step 1 is 30 minutes; the stirring and emulsifying time after adding vinyl acetate monomer is 30 minutes; the blue light appears Afterwards, the temperature was continued to rise to 80° C. for 30 minutes for the reaction.

进一步的,步骤二所述剩余的醋酸乙烯酯单体和丙烯酸丁酯单体的混合物的滴加速度为0.3~0.5mL/min。Further, the dropping rate of the mixture of the remaining vinyl acetate monomer and butyl acrylate monomer described in step 2 is 0.3-0.5 mL/min.

进一步的,步骤二所述引发剂分批补加所间隔的时间为30min。Further, the interval between batch addition of the initiator described in step 2 is 30 minutes.

进一步的,步骤二所述接枝单体的滴加速度为0.7~0.8mL/min。Further, the addition rate of the grafted monomer in step 2 is 0.7-0.8 mL/min.

进一步的,步骤二所述苯乙烯壳单体的滴加速度为0.1~0.4mL/min;所述升温至85℃后的保温时间为10min。Further, the dropping rate of the styrene shell monomer in step 2 is 0.1-0.4 mL/min; the holding time after the temperature is raised to 85° C. is 10 min.

进一步的,步骤二所述NMA功能单体的滴加速度为0.1~0.2mL/min,所述升温至80℃后的保温时间为30min。Further, the dropping rate of the NMA functional monomer in step 2 is 0.1-0.2 mL/min, and the holding time after the temperature is raised to 80° C. is 30 min.

本发明的有益效果:Beneficial effects of the present invention:

一、本发明提供的NMA改性聚醋酸乙烯酯基反向核壳结构乳液中的复合乳胶粒以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳,并在复合乳胶粒表面添加有功能单体NMA,本发明乳液胶黏剂在保持聚醋酸乙烯酯乳液良好胶接性能和反向结构复合乳胶粒优良耐水热性能的同时,在很大程度上提高了乳液胶接试件压缩剪切湿强度。One, the composite latex particles in the NMA modified polyvinyl acetate base reverse core-shell structure emulsion provided by the present invention take polyvinyl acetate as the core, and the small polystyrene particles are the shells, and add function on the surface of the composite latex particles Monomer NMA, the emulsion adhesive of the present invention, while maintaining the good bonding performance of the polyvinyl acetate emulsion and the excellent hydrothermal resistance of the reverse structure composite latex particles, greatly improves the compression shear of the emulsion bonding test piece. wet strength.

二、本发明提供的NMA改性聚醋酸乙烯酯基反向核壳结构乳液的制备方法采用N-羟甲基丙烯酰胺(NMA)作为功能单体,通过接枝共聚,在聚醋酸乙烯酯(PVAc)基核壳复合乳胶粒的壳层引入可交联基团,由于NMA结构中氮原子上高活性羟甲基的存在,使PVAc基核壳复合乳胶粒具有交联能力,其分子链在一定条件下发生羟甲基反应,脱去一分子水形成互穿网状结构,NMA自身的这种自交联属性能有效地提高乳液的胶接湿强度,同时可以提高胶黏剂的初粘性,又由于NMA为亲水性基团,可以极大改善乳液对被胶接对象的润湿性。Two, the preparation method of NMA modified polyvinyl acetate base reverse core-shell structure emulsion provided by the invention adopts N-methylolacrylamide (NMA) as functional monomer, by graft copolymerization, in polyvinyl acetate ( The shell layer of PVAc-based core-shell composite latex particles introduces cross-linkable groups. Due to the presence of highly active hydroxymethyl groups on the nitrogen atoms in the NMA structure, the PVAc-based core-shell composite latex particles have cross-linking ability, and their molecular chains are in Under certain conditions, a methylol reaction occurs, and a molecule of water is removed to form an interpenetrating network structure. The self-crosslinking property of NMA itself can effectively improve the bonding wet strength of the emulsion, and at the same time improve the initial tack of the adhesive. , and because NMA is a hydrophilic group, it can greatly improve the wettability of the emulsion to the glued object.

三、本发明提供的NMA改性聚醋酸乙烯酯基反向核壳结构乳液型胶黏剂无毒无害、对环境无污染,可在室温下存储和固化,可以直接用作水性胶黏剂,广泛应用于纸张包装、家具制造、室内装修、地板铺设和胶合木材等领域。3. The NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion-type adhesive provided by the present invention is non-toxic and harmless, has no pollution to the environment, can be stored and cured at room temperature, and can be directly used as a water-based adhesive , Widely used in paper packaging, furniture manufacturing, interior decoration, floor laying and glued wood and other fields.

四、本发明提供的NMA改性聚醋酸乙烯酯基反向核壳结构乳液制备工艺简单,原材料价格低廉,制备以及生产使用成本低,所制备的复合乳胶粒大小均一,形貌规整,有利于提供更优良的乳液胶黏剂的胶接性能以及便于实际施胶。Four, the preparation process of NMA modified polyvinyl acetate base reverse core-shell structure emulsion provided by the present invention is simple, and raw material price is cheap, and preparation and production use cost are low, and the prepared composite latex particles are uniform in size and regular in appearance, which is beneficial to Provide better bonding properties of emulsion adhesives and facilitate actual sizing.

附图说明Description of drawings

图1为实施例2制得的NMA改性聚醋酸乙烯酯基反向核壳结构乳液样品的TEM图;Fig. 1 is the TEM figure of the NMA modified polyvinyl acetate base reverse core-shell structure emulsion sample that embodiment 2 makes;

图2为实施例2制得的NMA改性聚醋酸乙烯酯基反向核壳结构乳液样品的SEM图;Fig. 2 is the SEM figure of the NMA modified polyvinyl acetate base reverse core-shell structure emulsion sample that embodiment 2 makes;

图3为实施例2-4制得的不同NMA含量的改性聚醋酸乙烯酯基反向核壳结构乳液中复合乳胶粒的粒径分布图;Fig. 3 is the particle size distribution figure of composite latex particle in the modified polyvinyl acetate base reverse core-shell structure emulsion of the different NMA content that embodiment 2-4 makes;

图4为实施例2制得的NMA改性聚醋酸乙烯酯基反向核壳结构乳液样品的红外光谱图;Fig. 4 is the infrared spectrogram of the NMA modified polyvinyl acetate base reverse core-shell structure emulsion sample that embodiment 2 makes;

图5为实施例2-4和对比例1制得的不同NMA含量的聚醋酸乙烯酯基反向核壳结构乳液的剪切湿强度对比图;Fig. 5 is the shear wet strength comparative figure of the polyvinyl acetate-based reverse core-shell structure emulsion of the different NMA content that embodiment 2-4 and comparative example 1 make;

图6为不同沸水处理条件下实施例2-4制得的不同NMA含量的改性聚醋酸乙烯酯基反向核壳结构乳液的压缩剪切强度对比图。Fig. 6 is a comparison chart of compressive shear strength of modified polyvinyl acetate-based reverse core-shell structure emulsions with different NMA contents prepared in Examples 2-4 under different boiling water treatment conditions.

具体实施方式Detailed ways

下面结合实施例对本发明的技术方案做进一步的说明,但并不局限于此,凡是对本发明技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,均应涵盖在本发明的保护范围中。The technical solution of the present invention will be further described below in conjunction with the examples, but it is not limited thereto. Any modification or equivalent replacement of the technical solution of the present invention without departing from the spirit and scope of the technical solution of the present invention should be covered by the present invention within the scope of protection.

实施例1Example 1

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液,主要由醋酸乙烯酯、苯乙烯和功能单体NMA制成,所述乳液中的复合乳胶粒呈草莓型核壳结构,以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳,在所述复合乳胶粒表面添加有功能单体NMA。An NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion, mainly made of vinyl acetate, styrene and functional monomer NMA, the composite latex particles in the emulsion have a strawberry-shaped core-shell structure, with poly Vinyl acetate is the core, small polystyrene particles are the shell, and functional monomer NMA is added on the surface of the composite latex particles.

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液的制备方法步骤如下:A kind of preparation method step of NMA modified polyvinyl acetate base reverse core-shell structure emulsion is as follows:

按反应的醋酸乙烯酯单体和苯乙烯单体总量为基准计,按如下重量配比准备各原料:The total amount of vinyl acetate monomer and styrene monomer by reaction is based on the basis, and each raw material is prepared according to the following weight ratio:

步骤一、将NaHCO3和复合乳化剂加入一定质量的去离子水中,其中复合乳化剂由乳化剂PCA507和乳化剂PCA078组成,其中PCA507与PCA078的重量比为(1~2):(1~2),升温至60℃,搅拌30min后加入占醋酸乙烯酯单体总重量10~20%的醋酸乙烯酯单体,搅拌乳化30min后,加入占过硫酸铵总重量30~50%的过硫酸铵水溶液,过硫酸铵水溶液是用占去离子水总重量的10~15%的去离子水溶解配制而成,升温至65℃继续反应,待出现蓝光后继续升温至80℃,反应30min后制得核种子乳液;Step 1. Add NaHCO3 and composite emulsifier to a certain quality of deionized water, wherein the composite emulsifier is composed of emulsifier PCA507 and emulsifier PCA078, wherein the weight ratio of PCA507 to PCA078 is (1~2):(1~2) , heat up to 60°C, stir for 30 minutes, add vinyl acetate monomer accounting for 10-20% of the total weight of vinyl acetate monomer, stir and emulsify for 30 minutes, add ammonium persulfate aqueous solution accounting for 30-50% of the total weight of ammonium persulfate , the ammonium persulfate aqueous solution is prepared by dissolving 10-15% of the total weight of deionized water. It is heated to 65°C to continue the reaction. After the blue light appears, continue to heat up to 80°C. seed emulsion;

步骤二、将步骤一制得的核种子乳液维持反应温度为80℃,逐滴滴加剩余的醋酸乙烯酯单体和丙烯酸丁酯单体的混合物到上述核种子乳液中,滴加速度为0.3~0.5mL/min,此滴加过程中,等量分批补加剩余的过硫酸铵,分批补加所间隔的时间为30min;待核单体混合物滴加完毕后,将马来酸酐单体滴加入反应体系中,马来酸酐单体是用占去离子水总重量的5~10%的去离子水溶解配制而成,滴加速度为0.7~0.8mL/min,待马来酸酐单体滴加完毕后马上开始滴加苯乙烯壳单体,苯乙烯壳单体的滴加速度为0.1~0.4mL/min,待苯乙烯壳单体滴加完毕后,升温至85℃,保温10min后将乳液降温至60℃,此时开始滴加一定比例的NMA功能单体,NMA功能单体的滴加速度为0.1~0.2mL/min,NMA功能单体滴加完毕后升温至80℃,保温30min后将反应体系自然冷却至室温,过滤,得到NMA改性聚醋酸乙烯酯基反向核壳结构乳液。Step 2. Maintain the reaction temperature of the nuclear seed emulsion prepared in step 1 at 80° C., dropwise add the mixture of the remaining vinyl acetate monomer and butyl acrylate monomer to the above-mentioned nuclear seed emulsion at a rate of 0.3- 0.5mL/min, during this dropping process, add the remaining ammonium persulfate in equal amounts in batches, and the interval between adding in batches is 30min; Add dropwise into the reaction system. The maleic anhydride monomer is prepared by dissolving 5-10% of the total weight of deionized water. The dropping rate is 0.7-0.8mL/min. Immediately after the addition of the styrene shell monomer, start to drop the styrene shell monomer. The dropping rate of the styrene shell monomer is 0.1-0.4mL/min. Cool down to 60°C, start to drop a certain proportion of NMA functional monomers at this time, the dropping rate of NMA functional monomers is 0.1-0.2mL/min, after the addition of NMA functional monomers, raise the temperature to 80°C, and keep warm for 30min. The reaction system was naturally cooled to room temperature, and filtered to obtain an NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion.

实施例2Example 2

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液,主要由醋酸乙烯酯、苯乙烯和功能单体NMA制成,所述乳液中的复合乳胶粒呈草莓型核壳结构,以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳,在所述复合乳胶粒表面添加有功能单体NMA。An NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion, mainly made of vinyl acetate, styrene and functional monomer NMA, the composite latex particles in the emulsion have a strawberry-shaped core-shell structure, with poly Vinyl acetate is the core, small polystyrene particles are the shell, and functional monomer NMA is added on the surface of the composite latex particles.

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液的制备方法步骤如下:A kind of preparation method step of NMA modified polyvinyl acetate base reverse core-shell structure emulsion is as follows:

按反应的醋酸乙烯酯单体和苯乙烯单体总量为基准计,按如下重量配比准备各原料:The total amount of vinyl acetate monomer and styrene monomer by reaction is based on the basis, and each raw material is prepared according to the following weight ratio:

步骤一、将NaHCO3和复合乳化剂加入一定质量的去离子水中,其中复合乳化剂由乳化剂PCA507和乳化剂PCA078组成,PCA507与PCA078的重量比为1:1,升温至60℃,搅拌30min后加入占醋酸乙烯酯单体总重量10%的醋酸乙烯酯单体,搅拌乳化30min后,加入占过硫酸铵总重量30%的过硫酸铵水溶液,过硫酸铵水溶液是用占去离子水总重量的12%的去离子水溶解配制而成,升温至65℃继续反应,待出现蓝光后继续升温至80℃,反应30min后制得核种子乳液;Step 1. Add NaHCO3 and composite emulsifier to a certain quality of deionized water, wherein the composite emulsifier is composed of emulsifier PCA507 and emulsifier PCA078, the weight ratio of PCA507 and PCA078 is 1:1, heat up to 60°C, and stir for 30 minutes Add vinyl acetate monomer accounting for 10% of the total weight of vinyl acetate monomer, stir and emulsify for 30 minutes, then add ammonium persulfate aqueous solution accounting for 30% of the total weight of ammonium persulfate, the ammonium persulfate aqueous solution is the total weight of deionized water It is prepared by dissolving 12% of deionized water, and the temperature is raised to 65°C to continue the reaction. After the blue light appears, the temperature is continued to rise to 80°C, and the nuclear seed emulsion is prepared after 30 minutes of reaction;

步骤二、将步骤一制得的核种子乳液维持反应温度为80℃,逐滴滴加剩余的90%醋酸乙烯酯单体和丙烯酸丁酯单体的混合物到上述核种子乳液中,滴加速度为0.3mLmin,此滴加过程中,等量分批补加剩余的70%的过硫酸铵,分批补加所间隔的时间为30min;待核单体混合物滴加完毕后,将马来酸酐单体滴加入反应体系中,马来酸酐单体是用占去离子水总重量的6%的去离子水溶解配制而成,滴加速度为0.7mL/min,待马来酸酐单体滴加完毕后马上开始滴加苯乙烯壳单体,滴加速度为0.2mL/min,待苯乙烯壳单体滴加完毕后,升温至85℃,保温10min后将乳液降温至60℃,此时开始滴加NMA功能单体,使NMA含量为醋酸乙烯酯单体和苯乙烯单体总重量的1.0%,NMA功能单体的滴加速度为0.1mL/min,NMA功能单体滴加完毕后升温至80℃,保温30min后将反应体系自然冷却至室温,过滤得到NMA含量为1.0%的改性聚醋酸乙烯酯基反向核壳结构乳液(CSN1)。Step 2, the nuclear seed emulsion that step 1 is made maintains reaction temperature to be 80 ℃, the mixture of remaining 90% vinyl acetate monomer and butyl acrylate monomer is added dropwise in the above-mentioned nuclear seed emulsion, and the rate of addition is 0.3mLmin, during this dropwise addition process, add the remaining 70% ammonium persulfate in equal amounts in batches, and the interval between adding in batches is 30min; Add the maleic anhydride monomer dropwise to the reaction system. The maleic anhydride monomer is prepared by dissolving 6% of the total weight of the deionized water. The dropping rate is 0.7mL/min. After the maleic anhydride monomer is added dropwise Immediately start adding the styrene shell monomer dropwise at a rate of 0.2mL/min. After the dropwise addition of the styrene shell monomer is complete, raise the temperature to 85°C, keep the temperature for 10 minutes and cool the emulsion down to 60°C, then start adding NMA dropwise Functional monomer, make NMA content be 1.0% of vinyl acetate monomer and styrene monomer gross weight, the rate of addition of NMA functional monomer is 0.1mL/min, be warming up to 80 ℃ after NMA functional monomer is added dropwise, After 30 min of heat preservation, the reaction system was naturally cooled to room temperature, and filtered to obtain a modified polyvinyl acetate-based reverse core-shell structure emulsion (CSN1) with an NMA content of 1.0%.

实施例3Example 3

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液,主要由醋酸乙烯酯、苯乙烯和功能单体NMA制成,所述乳液中的复合乳胶粒呈草莓型核壳结构,以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳,在所述复合乳胶粒表面添加有功能单体NMA。An NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion, mainly made of vinyl acetate, styrene and functional monomer NMA, the composite latex particles in the emulsion have a strawberry-shaped core-shell structure, with poly Vinyl acetate is the core, small polystyrene particles are the shell, and functional monomer NMA is added on the surface of the composite latex particles.

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液的制备方法步骤如下:A kind of preparation method step of NMA modified polyvinyl acetate base reverse core-shell structure emulsion is as follows:

按反应的醋酸乙烯酯单体和苯乙烯单体总量为基准计,按如下重量配比准备各原料:The total amount of vinyl acetate monomer and styrene monomer by reaction is based on the basis, and each raw material is prepared according to the following weight ratio:

步骤一、将NaHCO3和复合乳化剂加入一定质量的去离子水中,其中复合乳化剂由乳化剂PCA507和乳化剂PCA078组成,PCA507与PCA078的重量比为1:2,升温至60℃,搅拌30min后加入占醋酸乙烯酯单体总重量15%的醋酸乙烯酯单体,搅拌乳化30min后,加入占过硫酸铵总重量40%的过硫酸铵水溶液,过硫酸铵水溶液是用占去离子水总重量的13%的去离子水溶解配制而成,升温至65℃继续反应,待出现蓝光后继续升温至80℃,反应30min后制得核种子乳液;Step 1. Add NaHCO3 and composite emulsifier to a certain quality of deionized water, wherein the composite emulsifier is composed of emulsifier PCA507 and emulsifier PCA078, the weight ratio of PCA507 and PCA078 is 1:2, heat up to 60°C, and stir for 30 minutes Add vinyl acetate monomer accounting for 15% of the total weight of vinyl acetate monomer, stir and emulsify for 30 minutes, then add ammonium persulfate aqueous solution accounting for 40% of the total weight of ammonium persulfate, the ammonium persulfate aqueous solution is the total weight of deionized water It is prepared by dissolving 13% of deionized water, and the temperature is raised to 65°C to continue the reaction. After the blue light appears, the temperature is continued to rise to 80°C, and the nuclear seed emulsion is prepared after 30 minutes of reaction;

步骤二、将步骤一制得的核种子乳液维持反应温度为80℃,逐滴滴加剩余的85%醋酸乙烯酯单体和丙烯酸丁酯单体的混合物到上述核种子乳液中,滴加速度为0.4mL/min,此滴加过程中,等量分批补加剩余的60%的过硫酸铵,分批补加所间隔的时间为30min;待核单体混合物滴加完毕后,将马来酸酐单体滴加入反应体系中,马来酸酐单体是用占去离子水总重量的7%的去离子水溶解配制而成,滴加速度为0.75mL/min,待马来酸酐单体滴加完毕后马上开始滴加苯乙烯壳单体,滴加速度为0.3mL/min,待苯乙烯壳单体滴加完毕后,升温至85℃,保温10min后将乳液降温至60℃,此时开始滴加NMA功能单体,使NMA含量为醋酸乙烯酯单体和苯乙烯单体总量的2.0%,NMA功能单体的滴加速度为0.15mL/min,NMA功能单体滴加完毕后升温至80℃,保温30min后将反应体系自然冷却至室温,过滤得到NMA含量为2.0%的改性聚醋酸乙烯酯基反向核壳结构乳液(CSN2)。Step 2, the nucleus seed emulsion that step 1 is made maintains reaction temperature to be 80 ℃, the mixture of remaining 85% vinyl acetate monomer and butyl acrylate monomer is added dropwise in the above-mentioned nucleus seed emulsion, and the rate of addition is 0.4mL/min, during this dropping process, add the remaining 60% ammonium persulfate in equal amounts in batches, and the interval between adding in batches is 30min; The acid anhydride monomer is added dropwise in the reaction system. The maleic anhydride monomer is prepared by dissolving 7% of the total weight of deionized water in deionized water. The dropping rate is 0.75mL/min. Immediately after the addition of the styrene shell monomer, start dropping the styrene shell monomer at a rate of 0.3mL/min. After the addition of the styrene shell monomer is completed, raise the temperature to 85°C, keep the temperature for 10 minutes, and then cool the emulsion down to 60°C. Add NMA functional monomer, make NMA content be 2.0% of vinyl acetate monomer and styrene monomer total amount, the dropping rate of NMA functional monomer is 0.15mL/min, be warming up to 80 after NMA functional monomer is added dropwise ℃, after 30 min of heat preservation, the reaction system was naturally cooled to room temperature, and filtered to obtain a modified polyvinyl acetate-based reverse core-shell structure emulsion (CSN2) with an NMA content of 2.0%.

实施例4Example 4

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液,主要由醋酸乙烯酯、苯乙烯和功能单体NMA制成,所述乳液中的复合乳胶粒呈草莓型核壳结构,以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳,在所述复合乳胶粒表面添加有功能单体NMA。An NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion, mainly made of vinyl acetate, styrene and functional monomer NMA, the composite latex particles in the emulsion have a strawberry-shaped core-shell structure, with poly Vinyl acetate is the core, small polystyrene particles are the shell, and functional monomer NMA is added on the surface of the composite latex particles.

一种NMA改性聚醋酸乙烯酯基反向核壳结构乳液的制备方法步骤如下:A kind of preparation method step of NMA modified polyvinyl acetate base reverse core-shell structure emulsion is as follows:

按反应的醋酸乙烯酯单体和苯乙烯单体总量为基准计,按如下重量配比准备各原料:The total amount of vinyl acetate monomer and styrene monomer by reaction is based on the basis, and each raw material is prepared according to the following weight ratio:

步骤一、将NaHCO3和复合乳化剂加入一定质量的去离子水中,其中复合乳化剂由乳化剂PCA507和乳化剂PCA078组成,PCA507与PCA078的重量比为2:1,升温至60℃,搅拌30min后加入占醋酸乙烯酯单体总重量20%的醋酸乙烯酯单体,搅拌乳化30min后,加入占过硫酸铵总重量50%的过硫酸铵水溶液,过硫酸铵水溶液是用占去离子水总重量的14%的去离子水溶解配制而成,升温至65℃继续反应,待出现蓝光后继续升温至80℃,反应30min后制得核种子乳液;Step 1. Add NaHCO3 and composite emulsifier to a certain quality of deionized water, wherein the composite emulsifier is composed of emulsifier PCA507 and emulsifier PCA078, the weight ratio of PCA507 and PCA078 is 2:1, heat up to 60°C, and stir for 30 minutes Add vinyl acetate monomer accounting for 20% of the total weight of vinyl acetate monomer, stir and emulsify for 30 minutes, then add ammonium persulfate aqueous solution accounting for 50% of the total weight of ammonium persulfate, the ammonium persulfate aqueous solution is the total weight of deionized water It is prepared by dissolving 14% of deionized water, and the temperature is raised to 65°C to continue the reaction. After the blue light appears, the temperature is continued to rise to 80°C, and the nuclear seed emulsion is prepared after 30 minutes of reaction;

步骤二、将步骤一制得的核种子乳液维持反应温度为80℃,逐滴滴加剩余的80%醋酸乙烯酯单体和丙烯酸丁酯单体的混合物到上述核种子乳液中,滴加速度为0.5mL/min,此滴加过程中,等量分批补加剩余的50%的过硫酸铵,分批补加所间隔的时间为30min;待核单体混合物滴加完毕后,将马来酸酐单体滴加入反应体系中,马来酸酐单体是用占去离子水总重量的8%的去离子水溶解配制而成,滴加速度为0.8mL/min,待马来酸酐单体滴加完毕后马上开始滴加苯乙烯壳单体,滴加速度为0.4mL/min,待苯乙烯壳单体滴加完毕后,升温至85℃,保温10min后将乳液降温至60℃,此时开始滴加NMA功能单体,使NMA含量为醋酸乙烯酯单体和苯乙烯单体总量的3.0%,NMA功能单体的滴加速度为0.2mL/min,NMA功能单体滴加完毕后升温至80℃,保温30min后将反应体系自然冷却至室温,过滤得到NMA含量为3.0%的改性聚醋酸乙烯酯基反向核壳结构乳液(CSN3)。Step 2, the nuclear seed emulsion that step 1 is made maintains reaction temperature to be 80 ℃, the mixture of remaining 80% vinyl acetate monomer and butyl acrylate monomer is added dropwise in the above-mentioned nuclear seed emulsion, and the rate of addition is 0.5mL/min, during this dropwise addition process, add the remaining 50% ammonium persulfate in equal amounts in batches, and the interval between additions in batches is 30min; The acid anhydride monomer is added dropwise in the reaction system, and the maleic anhydride monomer is prepared by dissolving in deionized water accounting for 8% of the total weight of deionized water, and the dropping rate is 0.8mL/min. Immediately after the addition of the styrene shell monomer, drop the styrene shell monomer at a rate of 0.4mL/min. After the addition of the styrene shell monomer is complete, raise the temperature to 85°C, keep the temperature for 10 minutes, and cool the emulsion down to 60°C. Add NMA functional monomer, make NMA content be 3.0% of vinyl acetate monomer and styrene monomer total amount, the dropping speed of NMA functional monomer is 0.2mL/min, be warming up to 80 after NMA functional monomer is added dropwise ℃, after 30 min of heat preservation, the reaction system was naturally cooled to room temperature, and filtered to obtain a modified polyvinyl acetate-based reverse core-shell structure emulsion (CSN3) with an NMA content of 3.0%.

对比例1Comparative example 1

一种聚醋酸乙烯酯基反向核壳结构乳液,主要由醋酸乙烯酯和苯乙烯制成,所述乳液的复合乳胶粒呈草莓型核壳结构,以聚醋酸乙烯酯为核,聚苯乙烯小颗粒为壳。A polyvinyl acetate-based reverse core-shell structure emulsion, mainly made of vinyl acetate and styrene, the composite latex particles of the emulsion have a strawberry-shaped core-shell structure, with polyvinyl acetate as the core, polystyrene The small particles are shells.

一种聚醋酸乙烯酯基反向核壳结构乳液的制备方法步骤如下:A kind of preparation method step of polyvinyl acetate-based reverse core-shell structure emulsion is as follows:

按反应的醋酸乙烯酯单体和苯乙烯单体总量为基准计,按如下重量配比准备各原料:The total amount of vinyl acetate monomer and styrene monomer by reaction is based on the basis, and each raw material is prepared according to the following weight ratio:

步骤一、将NaHCO3和复合乳化剂加入一定质量的去离子水中,其中复合乳化剂由乳化剂PCA507和乳化剂PCA078组成,PCA507与PCA078的重量比为1:1,升温至60℃,搅拌30min后加入占醋酸乙烯酯单体总重量10%的醋酸乙烯酯单体,搅拌乳化30min后,加入占过硫酸铵总重量30%的过硫酸铵水溶液,过硫酸铵水溶液是用占去离子水总重量的12%的去离子水溶解配制而成,升温至65℃继续反应,待出现蓝光后继续升温至80℃,反应30min后制得核种子乳液;Step 1. Add NaHCO3 and composite emulsifier to a certain quality of deionized water, wherein the composite emulsifier is composed of emulsifier PCA507 and emulsifier PCA078, the weight ratio of PCA507 and PCA078 is 1:1, heat up to 60°C, and stir for 30 minutes Add vinyl acetate monomer accounting for 10% of the total weight of vinyl acetate monomer, stir and emulsify for 30 minutes, then add ammonium persulfate aqueous solution accounting for 30% of the total weight of ammonium persulfate, the ammonium persulfate aqueous solution is the total weight of deionized water It is prepared by dissolving 12% of deionized water, and the temperature is raised to 65°C to continue the reaction. After the blue light appears, the temperature is continued to rise to 80°C, and the nuclear seed emulsion is prepared after 30 minutes of reaction;

步骤二、将步骤一制得的核种子乳液维持反应温度为80℃,逐滴滴加剩余的90%醋酸乙烯酯单体和丙烯酸丁酯单体的混合物到上述核种子乳液中,滴加速度为0.3mL/min,此滴加过程中,等量分批补加剩余的70%的过硫酸铵,分批补加所间隔的时间为30min;待核单体混合物滴加完毕后,将马来酸酐单体滴加入反应体系中,马来酸酐单体是用占去离子水总重量的6%的去离子水溶解配制而成,滴加速度为0.7mL/min,待马来酸酐单体滴加完毕后马上开始滴加苯乙烯壳单体,滴加速度为0.2mL/min,待苯乙烯壳单体滴加完毕后,升温至85℃,保温10min后将反应体系自然冷却至室温,过滤得到未经NMA改性的聚醋酸乙烯酯基反向核壳结构乳液(CS)。Step 2, the nuclear seed emulsion that step 1 is made maintains reaction temperature to be 80 ℃, the mixture of remaining 90% vinyl acetate monomer and butyl acrylate monomer is added dropwise in the above-mentioned nuclear seed emulsion, and the rate of addition is 0.3mL/min, during this dropwise addition process, add the remaining 70% ammonium persulfate in equal amounts in batches, and the interval between batch additions is 30min; An acid anhydride monomer is added dropwise into the reaction system. The maleic anhydride monomer is prepared by dissolving 6% of the total weight of deionized water in deionized water. The dropping rate is 0.7mL/min. Immediately after the completion of the dropwise addition of the styrene shell monomer, the dropping rate was 0.2mL/min. After the dropwise addition of the styrene shell monomer was completed, the temperature was raised to 85°C, and after 10 minutes of heat preservation, the reaction system was naturally cooled to room temperature. Polyvinyl acetate-based reverse core-shell structure emulsion (CS) modified by NMA.

对NMA改性聚醋酸乙烯酯基反向核壳结构乳液的形貌表征:Morphological characterization of NMA-modified polyvinyl acetate-based reverse core-shell emulsion:

一、对实施例2制得的NMA含量为1.0%的改性聚醋酸乙烯酯基反向核壳结构乳液样品的形貌采用透射电镜(TEM)进行分析,通过重金属对乳液样品进行熏蒸染色,进一步验证复合乳胶粒核层与壳层的成分。聚苯乙烯易被重金属染色,因而在透射电镜下呈现深色,不易被重金属染色的聚醋酸乙烯酯则呈现浅色。由图1可以看出,核层呈现出浅色,而壳层呈现出深色,且深色部分是非连续的,呈点状分布在核层表面,这说明核为聚醋酸乙烯酯,外面的小颗粒为聚苯乙烯,从而证明本发明制备的复合乳胶粒是以聚醋酸乙烯酯为核,聚苯乙烯为壳的反向核壳结构。从图1可以看出复合乳胶粒粒径分布在150~300nm,且复合乳胶粒之间有粘连,使复合乳胶粒粒径增大。One, adopt the transmission electron microscope (TEM) to analyze the morphology of the modified polyvinyl acetate base reverse core-shell structure emulsion sample of 1.0% to the NMA content that embodiment 2 makes, carry out fumigation and dyeing to the emulsion sample by heavy metal, Further verify the composition of the core layer and the shell layer of the composite latex particle. Polystyrene is easily stained by heavy metals, so it appears dark under the transmission electron microscope, and polyvinyl acetate, which is not easily stained by heavy metals, appears light. It can be seen from Figure 1 that the core layer is light-colored, while the shell layer is dark-colored, and the dark-colored part is discontinuous and distributed on the surface of the core layer in the form of dots, which shows that the core is polyvinyl acetate, and the outer part is made of polyvinyl acetate. The small particles are polystyrene, thus proving that the composite latex particles prepared by the present invention take polyvinyl acetate as the core and polystyrene as the reverse core-shell structure of the shell. It can be seen from Figure 1 that the particle size distribution of the composite latex particles is between 150 and 300 nm, and there is adhesion between the composite latex particles, which increases the particle size of the composite latex particles.

二、对实施例2制得的NMA含量为1.0%的改性聚醋酸乙烯酯基反向核壳结构乳液样品的形貌采用扫描电镜(SEM)进行分析,如图2所示为稀释10000倍后的复合乳胶粒的扫描电镜图。由图2可以看出,乳液中的复合乳胶粒呈草莓型结构,以聚醋酸乙烯酯为核,其表面被直径为50~70nm的半球型聚苯乙烯颗粒所包覆。Two, the morphology of the modified polyvinyl acetate-based reverse core-shell structure emulsion sample with 1.0% NMA content prepared in Example 2 is analyzed by scanning electron microscope (SEM), as shown in Figure 2, it is diluted 10000 times Scanning electron micrograph of the composite latex particle after. It can be seen from Figure 2 that the composite latex particles in the emulsion have a strawberry-shaped structure, with polyvinyl acetate as the core, and its surface is covered by hemispherical polystyrene particles with a diameter of 50-70 nm.

三、图3为实施例2-4制得的不同NMA含量的改性聚醋酸乙烯酯基反向核壳结构乳液中复合乳胶粒的粒径分布图,横坐标表示粒径尺寸,纵坐标表示光强度;从图3可以看出当NMA含量1.0%时,复合乳胶粒平均粒径为157nm左右,乳液多分散系数为0.078,呈窄分布;提高NMA含量至2.0%时,乳液粒径基本不变,分布变窄,仍呈均一分布;进一步提高NMA的含量至3.0%时,乳胶粒粒径急剧增长,平均粒径为307.6nm,多分散系数变为0.111,粒径分布变宽。Three, Fig. 3 is the particle size distribution figure of composite latex particle in the modified polyvinyl acetate base reverse core-shell structure emulsion of the different NMA content that embodiment 2-4 makes, abscissa represents particle size, and ordinate represents Light intensity; As can be seen from Figure 3, when the NMA content was 1.0%, the average particle diameter of the composite latex particles was about 157nm, and the polydispersity coefficient of the emulsion was 0.078, showing a narrow distribution; When the content of NMA is further increased to 3.0%, the particle size of latex particles increases sharply, the average particle size is 307.6nm, the polydispersity coefficient becomes 0.111, and the particle size distribution becomes wider.

结合图1乳液样品中复合乳胶粒的TEM形貌表征可以说明在乳液体系中加入少量的NMA可以在复合乳胶粒壳层发生聚合反应,使复合乳胶粒粒径增大。当NMA含量过高时,则会导致复合乳胶粒之间的粘连、团聚,使得复合乳胶粒粒径急剧增长,较大的乳液粒径会对乳液的稳定性以及乳胶膜的致密性有较大影响,直接影响胶接产品的胶合质量。因此本发明在制备改性聚醋酸乙烯酯基反向核壳结构乳液时的NMA含量为1.0~3.5%。Combined with the TEM morphology characterization of the composite latex particles in the emulsion sample in Figure 1, it can be shown that adding a small amount of NMA to the emulsion system can cause polymerization in the shell of the composite latex particles, increasing the particle size of the composite latex particles. When the NMA content is too high, it will cause the adhesion and agglomeration between the composite latex particles, so that the particle size of the composite latex particles will increase sharply, and the larger particle size of the emulsion will have a greater impact on the stability of the emulsion and the compactness of the latex film. Influence, directly affect the glue quality of glued products. Therefore, the NMA content of the present invention is 1.0-3.5% when preparing the modified polyvinyl acetate-based reverse core-shell structure emulsion.

四、采用傅立叶红外光谱对实施例2制得的NMA改性聚醋酸乙烯酯基反向核壳结构乳液样品的化学结构进行分析,图4为实施例2制得的NMA改性聚醋酸乙烯酯基反向核壳结构乳液样品的红外光谱图;在3542cm-1、3456cm-1出现NMA特有结构伯酰胺双吸收峰;在1739cm-1出现醋酸乙烯酯上C=O伸缩振动特征吸收峰;1244cm-1处出现明显的醋酸乙烯酯、丙烯酸丁酯上C-O伸缩振动吸收峰。在758cm-1和694cm-1处出现属于苯乙烯中相邻的五个氢的面外弯曲振动峰。836cm-1处出现的尖峰为马来酸酐单体的双键打开形成-CH-CH-结构的面外弯曲振动吸收峰。通过以上红外谱图的对照可以明确地说明,在醋酸乙烯酯、丙烯酸丁酯、马来酸酐单体、苯乙烯以及NMA之间发生了复合。Four, adopt Fourier transform infrared spectrum to analyze the chemical structure of the NMA modified polyvinyl acetate base reverse core-shell structure emulsion sample that embodiment 2 makes, and Fig. 4 is the NMA modified polyvinyl acetate that embodiment 2 makes Infrared spectrogram of base reversed core-shell structure emulsion sample; NMA unique structural primary amide double absorption peaks appear at 3542cm -1 and 3456cm -1 ; C=O stretching vibration characteristic absorption peak on vinyl acetate appears at 1739cm -1 ; 1244cm Obvious absorption peaks of CO stretching vibration appear on vinyl acetate and butyl acrylate at -1 . Out-of-plane bending vibration peaks belonging to the adjacent five hydrogens in styrene appear at 758 cm −1 and 694 cm −1 . The sharp peak at 836cm -1 is the out-of-plane bending vibration absorption peak of the -CH-CH- structure formed by the opening of the double bond of the maleic anhydride monomer. Through the comparison of the above infrared spectra, it can be clearly demonstrated that the composite occurred between vinyl acetate, butyl acrylate, maleic anhydride monomer, styrene and NMA.

对实施例2-4制备的不同NMA含量的改性聚醋酸乙烯酯基反向核壳结构乳液和对比例1未经NMA改性的聚醋酸乙烯酯基反向核壳结构乳液的性能分析:The performance analysis of the modified polyvinyl acetate-based reverse core-shell structure emulsion of different NMA contents prepared in Examples 2-4 and the non-NMA-modified polyvinyl acetate-based reverse core-shell structure emulsion of Comparative Example 1:

一、图5为实施例2-4和对比例1制得的不同NMA含量的聚醋酸乙烯酯基反向核壳结构乳液的剪切湿强度对比图;由图5可知,对比例1未经NMA改性的空白对照乳液的剪切湿强度为0.90MPa,NMA含量为1.0%的聚醋酸乙烯酯基反向核壳结构乳液的剪切湿强度为1.05MPa,当NMA含量提高至2.0%时剪切湿强度上升至1.7MPa;继续提高NMA含量至3.0%时,剪切湿强度上升至2.6MPa,实施例4引入NMA后乳液剪切湿强度相比于对比例1提高了188.89%。NMA自身间发生脱水脱甲醛的自交联网状结构,提高了乳液的耐水性能;同时NMA中的羟甲基结构可以与木材中-COOH、-OH等形成氢键,提高乳液的剪切湿强度。One, Fig. 5 is the shear wet strength contrast figure of the polyvinyl acetate-based reverse core-shell structure emulsion of the different NMA content that embodiment 2-4 and comparative example 1 make; As can be seen from Fig. 5, comparative example 1 does not have The wet shear strength of the blank control emulsion modified by NMA is 0.90MPa, and the wet shear strength of the polyvinyl acetate-based reverse core-shell structure emulsion with 1.0% NMA content is 1.05MPa, when the NMA content is increased to 2.0% The wet shear strength rose to 1.7MPa; when the NMA content continued to increase to 3.0%, the wet shear strength rose to 2.6MPa, and the wet shear strength of the emulsion after introducing NMA in Example 4 increased by 188.89% compared with Comparative Example 1. The self-crosslinked network structure of dehydration and formaldehyde removal between NMA itself improves the water resistance of the emulsion; at the same time, the hydroxymethyl structure in NMA can form hydrogen bonds with -COOH, -OH in wood to improve the shear wet strength of the emulsion .

二、图6为不同沸水处理条件下实施例2-4制得的不同NMA含量的改性聚醋酸乙烯酯基反向核壳结构乳液的压缩剪切强度对比图;由图6可知,胶接试件经30min沸水煮后,NMA含量为0时,压缩剪切强度为0.04MPA;NMA含量为1.0%时,压缩剪切强度为0.07MPa;NMA含量升高至2.0%时,压缩剪切强度至0.043MPa;继续提高NMA含量至3.0%时,压缩剪切强度升高至0.13MPa。交接试件经180min沸水煮后,随着NMA含量升高,压缩剪切强度保持与30min沸水处理时相同的规律,呈现出先降低后升高的趋势。由此可以说明,经沸水处理后胶接试件仍保有一定的粘接强度。Tg代表分子链段解冻开始运动的温度,Tg以上温度条件使聚合物转变成高弹态,链段能够比较自由运动。聚醋酸乙烯酯的Tg为30~40℃之间,在高温的条件下会发生蠕变,短时间沸水条件下由于单体结构以及核壳结构等条件的协同效应,胶层未被完全破坏,因此NMA改性后的聚醋酸乙烯酯基乳液胶黏剂胶接的试件,经沸水处理后仍保有一定的粘接强度,且当NMA含量为3.0%时,其压缩剪切强度相对较高,由此证明本发明改性聚醋酸乙烯酯基反向核壳结构乳液经沸水处理后仍能保持较好的压缩剪切强度。Two, Fig. 6 is the compression shear strength comparison figure of the modified polyvinyl acetate base reverse core-shell structure emulsion of the different NMA content that embodiment 2-4 makes under different boiling water treatment conditions; After the specimen was boiled in boiling water for 30 minutes, when the NMA content was 0, the compressive shear strength was 0.04MPa; when the NMA content was 1.0%, the compressive shear strength was 0.07MPa; when the NMA content increased to 2.0%, the compressive shear strength to 0.043MPa; continue to increase the NMA content to 3.0%, the compressive shear strength increased to 0.13MPa. After the transfer specimens were boiled in boiling water for 180 minutes, as the NMA content increased, the compressive shear strength maintained the same law as that in the boiling water treatment for 30 minutes, showing a trend of first decreasing and then increasing. It can be shown that the bonded specimens still maintain a certain bonding strength after boiling water treatment. Tg represents the temperature at which the molecular chain segment thaws and starts to move. Temperatures above Tg make the polymer transform into a highly elastic state, and the chain segment can move relatively freely. The Tg of polyvinyl acetate is between 30 and 40°C, and it will creep under high temperature conditions. Due to the synergistic effect of the monomer structure and the core-shell structure and other conditions under the condition of boiling water for a short time, the glue layer is not completely destroyed. Therefore, the specimens bonded by NMA-modified polyvinyl acetate-based emulsion adhesive still retain a certain bonding strength after boiling water treatment, and when the NMA content is 3.0%, its compressive shear strength is relatively high , which proves that the modified polyvinyl acetate-based reverse core-shell structure emulsion of the present invention can still maintain good compressive shear strength after being treated with boiling water.

Claims (10)

1. a kind of reversed core-shell emulsion of NMA modified polyvinyl acetates base, it is characterised in that the NMA is modified poly-vinegar acid second The reversed core-shell emulsion of enester base is mainly made of vinylacetate, styrene and function monomer NMA, answering in the lotion Emulsion particle is closed in strawberry type nucleocapsid, using polyvinyl acetate as core, polystyrene little particle is shell, in the composite emulsion Grain surface is added with function monomer NMA.
A kind of 2. preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base, it is characterised in that the method Step is as follows:
Step 1: pH buffer and compound emulsifying agent are added in the deionized water of certain mass, 60 DEG C are warming up to, stirring is certain Added in after time and account for the Vinyl Acetate Monomer of Vinyl Acetate Monomer total weight 10~20%, stirring and emulsifying after a certain period of time, The initiator solution for accounting for initiator total weight 30~50% is added in, being warming up to 65 DEG C, the reaction was continued, continues after blue light to appear 80 DEG C are warming up to, semi-conducting materia lotion is made in reaction after a certain period of time;
Step 2: it is 80 DEG C that semi-conducting materia lotion made from step 1 is maintained reaction temperature, remaining vinyl acetate is added dropwise dropwise In the mixture of ester monomer and Butyl Acrylate Monomer to above-mentioned semi-conducting materia lotion, during this dropwise addition, equivalent is added surplus in batches Remaining initiator;After nuclear monomer mixture is added dropwise, grafted monomers are added dropwise in reaction system, monomer dropping to be grafted After start that styrene shell monomer is added dropwise at once, after styrene shell monomer is added dropwise, be warming up to 85 DEG C, one timing of heat preservation Between after lotion is cooled to 60 DEG C, start that a certain proportion of NMA function monomers are added dropwise at this time, after NMA function monomers are added dropwise 80 DEG C are warming up to, reaction system cooled to room temperature, filtering are obtained into NMA modified polyvinyl acetates after held for some time The reversed core-shell emulsion of ester group.
3. a kind of preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to claim 2, It is characterized in that based on the basis of the Vinyl Acetate Monomer of reaction and styrene monomer total amount, the weight proportion of each raw material used is such as Under:
4. a kind of preparation side of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to Claims 2 or 3 Method, it is characterised in that the pH buffer is NaHCO3;The compound emulsifying agent is by emulsifier PCA507 and emulsifier PCA078 The weight ratio of composition, wherein PCA507 and PCA078 are (1~2):(1~2);The initiator be ammonium persulfate, initiator water Solution is to be formulated ammonium persulfate with 10~15% deionized water dissolving for accounting for ionized water total weight;The grafting is single Body is maleic anhydride, and maleic anhydride monomer is that maleic anhydride is water-soluble with 5~10% deionization for accounting for ionized water total weight Solution is formulated.
5. a kind of preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to claim 4, It is characterized in that adding in pH buffer and compound emulsifying agent in deionized water described in step 1 and is warming up to the mixing time after 60 DEG C For 30min;The time of stirring and emulsifying is 30min after the addition Vinyl Acetate Monomer;It is described the subsequent temperature of continuing rising of blue light occur The time reacted to 80 DEG C is 30min.
6. a kind of preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to claim 5, The rate of addition for being characterized in that the mixture of remaining Vinyl Acetate Monomer and Butyl Acrylate Monomer described in step 2 is 0.3 ~0.5mL/min.
7. a kind of preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to claim 6, It is characterized in that initiator described in step 2 adds institute's interlude as 30min in batches.
8. a kind of preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to claim 7, The rate of addition for being characterized in that grafted monomers described in step 2 is 0.7~0.8mL/min.
9. a kind of preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to claim 8, The rate of addition for being characterized in that styrene shell monomer described in step 2 is 0.1~0.4mL/min;The guarantor being warming up to after 85 DEG C The warm time is 10min.
10. a kind of preparation method of the reversed core-shell emulsion of NMA modified polyvinyl acetates base according to claim 9, It is characterized in that the rate of addition of NMA function monomers described in step 2 be 0.1~0.2mL/min, it is described be warming up to 80 DEG C after Soaking time is 30min.
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