1)isobutene异丁烯
1.Operation optimum for isobutene production by methyl-tert-butyl ether cracking;甲基叔丁基醚裂解制异丁烯装置的操作优化
2.Research of isobutene oligomerization s catalyst using supporter of mordenite;以丝光沸石为载体的异丁烯齐聚反应催化剂的研究
3.Study of mesitylene preparing by alkylation of mix C_9 aromatic hydrocarbon and isobutene;混合C_9芳烃与异丁烯烷基化制备均三甲苯的研究
英文短句/例句
1.isobutylene-isoprene copolymer异丁烯－异戊二烯共聚物
2.MAA (methacrylic acid)甲基丙烯酸,异丁烯酸
3.polylauryl methacrylate聚十二基异丁烯酸盐
4.Systhesis of Copolymers of Isobutyl and Tert-butyl Acrylate by Cationic Polymerization and Atom Transfer Radical Polymerization;阳离子/ATRP合成异丁烯/丙烯酸叔丁酯共聚物研究
5.Isobutane Catalytic Dehydrogenation to Isobutylene on VO_x/SiO_2 CatalystsVO_x/SiO_2催化剂上异丁烷催化脱氢制异丁烯
6.A resin derived from methacrylic acid.异丁烯酸脂系树脂从异丁烯酸中提炼的一种树脂
7.The Feasibility of PIB Plant to Produce LPIB Product聚异丁烯装置生产低分子聚异丁烯产品的可行性
8.The Synthesis of Star-Branched Butyl Rubber and Star-Branched Polyisobutylene;星形支化丁基橡胶及星形支化聚异丁烯的合成
9.Study of Catalysts For Producing Isobutene By Decomposition of Methyl Tert-Butyl Ether;甲基叔丁基醚裂解制异丁烯催化剂的研究
10.Synthesis of Block Copolymer of Isobutylene and Styrene Coinitiated by AlCl_3;Al系共引发合成异丁烯和苯乙烯嵌段共聚物
11.Study for the Catalyst of the Isobutene Selection Oxidation for Methacrolein;异丁烯选择氧化制备甲基丙烯醛催化剂的研究
12.Industrial Production of High Purity Isobutene by MTBE Cracking Method;MTBE裂解法工业生产高纯度异丁烯技术
13.Partial Oxidation of Isobutene/tert-Butanol to Methacrolein on Mo-Bi-Co-Fe-based Complex Catalyst;Mo-Bi-Co-Fe基催化剂上异丁烯/叔丁醇部分催化氧化制甲基丙烯醛
14.butadiene isoprene copolymer丁二烯-异戊二烯共聚物
15.Study on the High Trans Butadiene-Isoprene Copolymer高反式丁二烯—异戊二烯共聚物的研究
16.STUDIES ON THE SYNTHESIS OF BUTADIENE/ISOPRENE/STYRENE POLYMER INITIATED BY DILITHIUM INITIATORS;双锂体系丁二烯/异戊二烯/苯乙烯聚合物的研制
17.The Terpolymerization of Styrene-butadiene-isoprene to Synthesize SIBR;苯乙烯—丁二烯—异戊二烯三元共聚合成SIBR
18.Study on a Novel Block Polymer Comprising Styrene, Butadiene and Isoprene;苯乙烯/丁二烯/异戊二烯新型嵌段聚合物的研究
相关短句/例句
Isobutylene[,ais?u'bju:tili:n]异丁烯
1.Studies on catalytic reaction of selective oxidation of isobutylene to methacrolein;异丁烯选择氧化制备甲基丙烯醛催化反应的研究
2.A Discussion on the Prospects of MTBE Production and Isobutylene Utilization(Ⅰ);利用异丁烯生产MTBE应用前景探讨(上)
3.A Discussion on the Prospects of MTBE Production and Isobutylene Utilization(Ⅱ);利用异丁烯生产MTBE应用前景探讨(下)
3)Isobutane/butene异丁烷/丁烯
1.Regeneration of Brnsted-Lewis Conjugated Solid Superacid in the Alkylation of Isobutane/butene;固体超强酸在异丁烷/丁烯烷基化反应中的再生研究
4)Polyisobutylene[p?li'ais?u'bju:tili:n]聚异丁烯
1.Disscusion Upon the Relation Between Low Molecular Weight Polyisobutylene and Its Kinematic Viscosity;低分子聚异丁烯与其运动粘度关系探讨
2.Detection of polyisobutylene in polyisobutylene succinic anhydride by HPLC;聚异丁烯丁二酸酐中聚异丁烯的液相色谱分析
3.Study on the Catalysts for Polyisobutylene with a Terminal Double Bond;高端基烯烃聚异丁烯催化剂研究
5)polyisobutene聚异丁烯
1.Development of investigation and process optimization on polyisobutene;聚异丁烯研究进展及其工艺优化
2.Research of Determining High Active End Group Content and Molecular Weight of Polyisobutene;聚异丁烯高活性端基含量及相对分子质量测定方法的研究
3.nC_6H_(14)—CH_2Cl_2 Volumn ratio influene on molecular weight and formation of polyisobutene with BF_3;正己烷—二氯甲烷溶剂配比对BF_3引发体系聚异丁烯分子量及结构影响的研究
6)diisobutene二异丁烯
1.With diisobutene form polyunit as feedstock, hydrogenation reaction is made in the fixed bed hydrogenation unit, isooctane is produced by diisobutene hydrogenation under proper reaction condition and in the presence of hydrogenation catalyst, the purity of isooctane so produced is 93%, and can reach 99.利用叠合装置的二异丁烯为原料,在固定床加氢装置上进行加氢反应,在适宜的反应条件和加氢催化剂作用下,二异丁烯加氢生成异辛烷,所得异辛烷纯度为93%,再经分馏进行提纯,可得到纯度为99。
2.MTBE and diisobutene are important intermediates of downstream C4 petrochemical products.石家庄炼油工股份有限公司采用MTBE联产二异丁烯技术,创造性地将生产MTBE与生产二异丁烯两种不同的工艺技术进行了融合,大幅度提高了原有装置的盈利能力。
3.In order to solve the problems such as multiple components in products, long time of rectification, high energy consumption, low yield and purity of product occurring during the production of p - octyl phenol, the effects of reaction conditions including reaction temperature, reaction time, the molar ratio of phenol to diisobutene on the conversion and yield of the product were examined.为解决对辛基酚生产过程中精馏时存在组分多、精馏时间长、能耗高、产品收率和纯度低等问题,用正交实验探讨反应温度、反应时间、苯酚与二异丁烯原料摩尔比3因素对原料转化率和产品对辛基酚收率的影响。
延伸阅读
异丁烯 (CH3)2C＝CH2 又称2-甲基丙烯。易燃、易爆气体(爆炸极限1.7％～9.0％体积)，沸点-6.90°C,临界温度144.75°C，临界压力4.00MPa。工业上,异丁烯几乎都是由炼厂气和裂解C4馏分（见碳四馏分）中获得。炼厂气中异丁烯的含量一般为5％～12％,裂解C4馏分中一般为20％～30％。少数情况下用氧化铬－氧化铝催化剂由异丁烷催化脱氢而制得。以丙烯和异丁烷为原料用共氧化法生产环氧丙烷时，异丁烯是其联产物。 由碳四馏分分离异丁烯，通常是在先分出其中的丁二烯以后进行的。最常用的分离异丁烯方法是硫酸吸收法，所得异丁烯纯度>99％,回收率达92％。分子筛吸附法，采用一定孔径范围（约3～10┱）的分子筛，从C4馏分抽余液中选择性地分离出丁烯及正丁烷，所得异丁烯纯度达99％。离子交换树脂法也可得高纯度异丁烯，但因反应效率低，应用不广。此外，还有以阳离子交换树脂为催化剂，以甲醇与C4馏分中异丁烯反应生成甲基叔丁基醚，以及在酸性催化剂作用下将异丁烯齐聚生成二异丁烯及异丁烯的三聚物，从而与C4馏分抽余液中的其他组分分离等方法。甲基叔丁基醚法较有前途（见碳四馏分分离）。 工业上高浓度异丁烯主要用于生产聚异丁烯以及和异戊二烯共聚生产丁基橡胶。异丁烯与异丁烷进行烷基化反应，可生产高辛烷值烷基化汽油，与甲醇反应所得甲基叔丁基醚是优良的汽油添加剂，齐聚所得二聚物及三聚物经加氢后是汽化器燃料的添加剂，也适用于作芳烃的烷基化原料。二异丁烯还可作为羰基合成的原料生产异壬醇，进一步制造增塑剂。此外，异丁烯可经氧化得甲基丙烯酸，经氨化氧化得甲基丙烯腈，再水合可制得叔丁醇。
