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Multistage process for production of graft modified olefin polymers useful for adhesive coatings on metallic and other surfaces, compatibility improver in polymer molding compositions, and reactive coupling agent in polymer composites

机译:用于接枝改性的烯烃聚合物的多阶段生产方法,可用于金属和其他表面的粘合剂涂层,聚合物模塑组合物中的相容性改进剂以及聚合物复合材料中的反应性偶联剂

摘要

A multistage process for production of graft modified olefin polymers of functionality 0.1-5 wt.% involves: (i) heating reaction mixture containing olefin polymer, butyl acrylate (BA) and peroxide; (ii) reacting of BA or BA/comonomer mixture; (iii) adding maleic acid anhydride (MAA) or MAA mixture, and heating; (iv) blowing with nitrogen; (v) removing unreacted monomer; and (vi) cooling and removing the product. A multistage process for production of graft modified olefin polymers of functionality 0.1-5 wt.% involving: (i) heating reaction mixture containing (wt.%): particulate olefin polymer or olefin polymer blend (60-97) of mean particle diameter 0.01-8 mm, butyl acrylate (BA)(2-24) or BA/comonomer mixture in weight ratio at least 1 part BA per part comonomer, organic peroxide (1-16) or a mixture of at least two organic peroxides of half life 2-150 minutes at a selected reaction temperature (TR1 and TR2) as radical former, weight ratio of BA or BA/comonomer mixture to radical former 0.2-20, dispersion temperature TD1 between room temperature TN and 60 degreesC, dispersion time 1-150 minutes; (ii) heating the mixture within a time tA1 of 5-200 minutes from the dispersion temperature TD1 to the reaction temperature TR1 of 60-130 degreesC, (iii) reacting BA or the BA/comonomer mixture at TR1 of 60-130 degreesC within a reaction time tR1 of 5-300 minutes with maintenance of a solid (dry) consistency in the reaction mixture, and after a monomer conversion of 50-99% in a second state; (iv) adding maleic acid anhydride (MAA) or MAA/comonomer mixture corresponding to a composition MAA (20-95)/comonomer (5-80) at a temperature in the TR1 region, with dispersion within a time tD2 of 1-150 minutes; (v) after a heating time tA2 of 5-200 minutes, heating to a reaction temperature TR2 of 100-160 degreesC; and (vi) reaction with maintenance of TR2 with the reaction time tR2 of 5-300 minutes and the reaction mixture in the solid (dry) state; (vii) removing unreacted monomer from the reaction mixture which is blown with nitrogen over a desorption time tdes of 20-240 minutes and a desorption temperature TDes between reaction temperature TR2 and 80 degreesC, the residual initiator is deactivated and after cooling to a final temperature between 80 degreesC and room temperature TN the dry graft modified olefin polymer or olefin polymer blend is removed.
机译:生产官能度为0.1-5重量%的接枝改性的烯烃聚合物的多阶段方法包括:(i)加热包含烯烃聚合物,丙烯酸丁酯(BA)和过氧化物的反应混合物; (ii)使BA或BA /共聚单体混合物反应; (iii)加入马来酸酐(MAA)或MAA混合物,并加热; (iv)用氮气吹气; (v)除去未反应的单体; (vi)冷却并取出产品。生产官能度为0.1-5 wt。%的接枝改性烯烃聚合物的多阶段方法,涉及:(i)加热反应混合物,其中包含(wt。%):颗粒烯烃聚合物或烯烃聚合物共混物(60-97),平均粒径0.01 -8毫米丙烯酸丁酯(BA)(2-24)或BA /共聚单体混合物,重量比为每份共聚单体至少1份BA,有机过氧化物(1-16)或至少两种半衰期有机过氧化物的混合物在选定的反应温度(TR1和TR2)作为自由基形成剂的情况下放置2至150分钟,BA或BA /共聚单体混合物与自由基形成剂的重量比为0.2-20,室温TN和60摄氏度之间的分散温度TD1,分散时间1-150分钟; (ii)在从分散温度TD1开始的5-200分钟的时间tA1内将混合物加热至60-130℃的反应温度TR1,(iii)使BA或BA /共聚单体混合物在60-130℃的TR1下反应。反应时间tR1为5-300分钟,同时保持反应混合物中的固体(干)稠度,并且在第二状态下单体转化率为50-99%之后; (iv)在TR1区域的温度下加入马来酸酐(MAA)或对应于MAA(20-95)/共聚单体(5-80)组成的MAA /共聚单体混合物,在时间tD2为1-150内分散分钟; (v)在5-200分钟的加热时间tA2之后,加热到100-160℃的反应温度TR2; (vi)在维持TR2的条件下进行反应,其中反应时间tR2为5-300分钟,反应混合物为固态(干燥)。 (vii)从反应混合物中除去未反应的单体,该反应混合物在20-240分钟的解吸时间tdes和反应温度TR2与80℃之间的解吸温度TDes下用氮气吹送,使残余的引发剂失活,并冷却至最终温度后在80℃和室温TN之间,除去干接枝改性的烯烃聚合物或烯烃聚合物共混物。

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