1) molybdenum polyisobutenyl succinate (MoPIBS)
聚异丁烯基丁二酰钼
2) polyisobutylene succinimide
聚异丁烯丁二酰亚胺
1.
The emission amount of tail gas in polyisobutylene succinimide production is very large,and the concentration of oil in the recovered chlorhydric acid by absorption is too high to sell.
针对聚异丁烯丁二酰亚胺生产工艺中废气排放量大、尾气吸收得到的盐酸含油量高、难以销售等问题,在分析原因的基础上,对尾气吸收系统进行了技术改进。
2.
An improved process for producing polyisobutylene succinimide used in emulsion explosive was introduced.
介绍了一种经过改进的乳化炸药用聚异丁烯丁二酰亚胺的生产工艺。
3) polyisobutylene-bis-succinimide
聚异丁烯双丁二酰亚胺
1.
The technological character of using polyisobutylene-bis-succinimide as emulsifier in emulsion explosive were researched.
研究了聚异丁烯双丁二酰亚胺作为乳化炸药乳化剂的技术特点 ,并同常用乳化剂Span 80作了比较。
4) methacryl(o)yl-; methylacryloyl
异丁烯酰(基)
5) diisobutylene
[dai,aisə'butili:n]
二聚异丁烯
1.
Result showed that conversion of isobutylene reached 80% and selectivity of diisobutylene was 90% when reacted at 180 oC with mass airspeed of 3h-1 by self-made R2 catalyst.
利用分子筛催化异丁烯合成二聚异丁烯,在固定床反应器中考查了温度、空速对异丁烯齐聚反应的影响。
2.
p-tert-Octylphenol(PTOP) was synthesized from phenol and diisobutylene(DIB),which was a distillate of butene oligomer from Lanzhou Refinery.
从兰州炼油厂的C_4烯烃齐聚物中精馏分离出二聚异丁烯,再与苯酚进行烷基化反应合成了对叔辛基酚(PTOP);筛选出可用的催化剂C101阳离子交换树脂,并优选出反应最佳工艺条件:反应温度80℃,反应时间6 h,叫(催化剂)=0。
3.
This paper examines the alternating copolymerization of diisobutylene-maleicanhydride monomers in the presense of initiator through solution polymerization.
以二聚异丁烯,马来酸酐为主要单体,在引发剂存在下,采用溶液聚合方法,合成了具有交替结构的共聚物(IBMA-2),研究了聚合配方及合成工艺条件对产物收率,分子量等影响,通过元素分析,测定了原料配比、转化率与共聚物组成的关系,结果表明,该共聚物具有近似交替结构的特征。
6) poly(N-vinylisobutyramide)
聚N-乙烯基异丁酰胺
补充资料：二氯化异丁烯
分子式：(CH3)2CClCH2CL
CAS号：
性质：又称二氯化异丁烯。液体。沸点106.5℃(常压),59～60℃(19.998kPa)。密度d201.093g/cm3。折射率nD201.4370。与氢氧化钾共热,则生成异丁二醇。可由氯异丁烷在三氯化铝存在下,于低温时与氯反应制取。用作有机合成原料。
CAS号：
性质：又称二氯化异丁烯。液体。沸点106.5℃(常压),59～60℃(19.998kPa)。密度d201.093g/cm3。折射率nD201.4370。与氢氧化钾共热,则生成异丁二醇。可由氯异丁烷在三氯化铝存在下,于低温时与氯反应制取。用作有机合成原料。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条