.;EFFECT: invention allows to increase duration of active state of the catalytic system, which leads to increase in MM value and increase in the yield of UHMWPE based on the loaded complex with increase in the polymerization duration of more than 1 hour.;1 cl, 9 ex"/> METHOD OF PREPARING CATALYST SYSTEM FOR PRODUCTION OF REACTOR POWDER OF ULTRA-HIGH MOLECULAR WEIGHT POLYETHYLENE
首页> 外国专利> METHOD OF PREPARING CATALYST SYSTEM FOR PRODUCTION OF REACTOR POWDER OF ULTRA-HIGH MOLECULAR WEIGHT POLYETHYLENE

METHOD OF PREPARING CATALYST SYSTEM FOR PRODUCTION OF REACTOR POWDER OF ULTRA-HIGH MOLECULAR WEIGHT POLYETHYLENE

机译:一种制备超高分子量聚乙烯反应粉的催化剂体系的制备方法

摘要

FIELD: manufacturing technology; chemistry.;SUBSTANCE: invention relates to production of polyethylene, namely to method for producing a reactor powder of UHMWPE by polymerization of ethylene. In the process, the reaction of bis{2-[(4-allyloxyphenylimino)methyl]-4-R2-6-R1-phenoxy} titanium (IV) dichloride complexes (I)…(XIX) with organoaluminum MAO activator is carried out in the presence of ethylene dissolved in the reaction medium before the addition of the complex. Method includes step of mixing certain amounts of toluene, MAO solution in toluene, saturation of mixture with ethylene, followed by introduction of a solution of one of said group of complexes (I)…(XIX) in toluene, “maturing” stage of the system obtained at the mixing stage, carried out at a temperature of 10–80 °C, preferably 20–60 °C, both at the same temperature and at different temperatures for each stage, at an ethylene pressure of 0.01–8 atm, preferably below 1 ati, both at the same and different pressure for each stage, at the concentration of the complex in the catalyst system obtained in the “maturing” stage, ranging from 0.1 to 60 mcmol/l, preferably from 10 to 40 mcmol/l, and Al/Ti ratio of 50–1500, preferably 100–1000, and ethylene polymerization step carried out at a temperature of 10–80 °C, preferably 20–60 °C, ethylene pressure of 1–8 atm, preferably 2–5 atm, a duration of the polymerization process ranging from 10 minutes to 8 hours, preferably from 30 minutes to 5 hours, the rotational speed of the blade mixer is 50–2000 rpm, preferably 100–1000 rpm. Complexes (I)…(XIX) contain such combinations of substituents R1 and R2 as R1= t-Bu, R2=H (I); R1=R2=t-Bu (II); R1=t-Bu, R2=Me (III); R1=t-Bu, R2=OMe (IV); R1=t-Bu, R2=CMe2(Ph) (V); R1=CMe2(Ph), R2=H (VI); R1=R2=CMe2(Ph) (VII); R1=CMe2(Ph), R2=Me (VIII); R1=CMe2(Ph), R2=t-Bu (IX); R1=CMe2(Ph), R2=OMe (X); R1=CHMe(Ph), R2=H (XI); R1=CHMe(Ph), R2=Me (XII); R1=CHMe(Ph), R2=OMe (XIII); R1=CHMe(C6H4-4-t-Bu), R2=H (XIV); R1=CHMe(C6H4-4-t-Bu), R2=Me (XV); R1=CHMe(C6H4-4-t-Bu), R2=OMe (XVI); R1=2-isobornyl, R2=H (XVII); R1=2-isobornyl, R2=Me (XVIII); R1=2-isobornyl, R2=OMe (XIX). ; .;EFFECT: invention allows to increase duration of active state of the catalytic system, which leads to increase in MM value and increase in the yield of UHMWPE based on the loaded complex with increase in the polymerization duration of more than 1 hour.;1 cl, 9 ex
机译:领域:制造技术;化学领域;本发明涉及聚乙烯的生产,即涉及通过乙烯聚合生产UHMWPE的反应器粉末的方法。在此过程中,双{2-[(4-烯丙氧基苯基亚氨基)甲基] -4-R 2 -6-R 1 -苯氧基}钛(IV)反应在加入络合物之前,在溶解于反应介质的乙烯存在下,进行带有有机铝MAO活化剂的二氯化物络合物(I)…(XIX)。该方法包括以下步骤:混合一定量的甲苯,MAO在甲苯中的溶液,将混合物与乙烯饱和,然后引入上述一组配合物(I)…(XIX)在甲苯中的溶液,该过程的“成熟”阶段在混合阶段获得的体系,温度为10–80°C,优选为20–60°C,每个阶段在相同温度和不同温度下进行,乙烯压力为0.01-8 atm,优选在“成熟”阶段获得的催化剂体系中,配合物的浓度在每个阶段的压力相同和不同时均低于1 ati,范围为0.1至60 mcmol / l,优选10至40 mcmol / l ,Al / Ti比为50-1500,优选100-1000,乙烯聚合步骤在10-80°C,优选20-60°C,乙烯压力1-8 atm,优选2-在5个大气压下,聚合过程的持续时间为10分钟至8小时,优选30分钟至5小时rs,叶片搅拌机的转速为50-2000 rpm,最好为100-1000 rpm。配合物(I)…(XIX)包含取代基R 1 和R 2 的组合,如R 1 = t-Bu,R 2 = H(I); R 1 = R 2 = t-Bu(II); R 1 = t-Bu,R 2 = Me(III); R 1 = t-Bu,R 2 = OMe(IV); R 1 = t-Bu,R 2 = CMe 2 (Ph)(V); R 1 = CMe 2 (Ph),R 2 = H(VI); R 1 = R 2 = CMe 2 (Ph)(VII); R 1 = CMe 2 (Ph),R 2 = Me(VIII); R 1 = CMe 2 (Ph),R 2 = t-Bu(IX); R 1 = CMe 2 (Ph),R 2 = OMe(X); R 1 = CHMe(Ph),R 2 = H(XI); R 1 = CHMe(Ph),R 2 = Me(XII); R 1 = CHMe(Ph),R 2 = OMe(XIII); R 1 = CHMe(C 6 H 4 -4-t-Bu),R 2 = H(十四); R 1 = CHMe(C 6 H 4 -4-t-Bu),R 2 = Me( XV); R 1 = CHMe(C 6 H 4 -4-t-Bu),R 2 = OMe( XVI); R 1 = 2-异冰片基,R 2 = H(XVII); R 1 = 2-异冰片基,R 2 = Me(XVIII); R 1 = 2-异冰片基,R 2 = OMe(XIX)。 ; <图像文件=“ 00000006.JPG” he =“ 87” imgContent =“未定义” imgFormat =“ JPEG” wi =“ 76” />。;效果:发明允许增加催化系统活性状态的持续时间,这导致聚合时间增加1小时以上,基于负载的配合物,MM值增加,UHMWPE收率增加。; 1 cl,9 ex

著录项

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号