• 基本释义

1.Improvement of selective hydrogenation catalysts for alkyne series in France
法国对炔烃选择加氢催化剂的改进收藏指正
2.The Synthesis of Terminal Hydroxy Alkyne Ⅱ.The Synthesis of 4-Alkyl-3-butyn-1-ol
末端羟基炔烃的合成——Ⅱ.4-烃基-3-丁-1-醇的合成(英文)收藏指正
3.Abstract: This article reviews recent progress in nucleophilic reactions of the α-carbon in vinylidene ruthenium complexes. The nucleophiles include alkene, alkyne, alcohol, acid, amine, water, etc.
文摘:综述了近几年钌亚乙烯基络合物中间体α-碳的亲核反应。亲核试剂包括烯烃、炔烃、醇、酸、胺、水等。收藏指正
4.SAA ligand Lh could induce asymmetric addition of terminal alkyne to aldehydes without using air-sensitive Ti(O~iPr)4and expensive Zn(OTf)2.with good result of high yield (up to 99%) and good enantioselectivities (up to 84%ee).
将SAA配体Lh应用于在无Ti(O~iPr)_4和Zn(OTf)_2的条件下促进端基对醛的不对称加成反应中,反应的收率普遍较高,最高达99%,对映体选择性高达84%ee。收藏指正
5.Based on characteristics and connectivity of the groups in molecules, the group contribution method and topological method was combined together, a new method was developed which can be used to calculate the density of alkyne from molecular structure.
摘要根据分子中基团的特性和连接性,将基团贡献法和拓扑方法结合在一起,发展了一种计算炔烃密度的新方法-基团键贡献法,该方法具有基团贡献法适用范围广和拓扑方法计算结果准确可靠的特点。收藏指正
6.Sulfony 13 oxybicyclo[9.3.0]tetradec 3,8 diyne is the precursor of the bicyclic enediyne which has been synthesized from cis 1,2,3,6 tetrahydropathalican hydride by 8 step reactions. We got the goal compound by reduction of anhydride, ozonolysis of 8 oxabicyclo[4.3.0]non 3 ene, Witting reaction with PPh 3/CBr 4, formation of alkyne and esterification, reduction of the ester, formation of the mesylate, cyclization with sodium sulfide nonhydrate.
以顺 - 1,2 ,3,6 -四氢邻苯二甲酸酐为原料 ,经还原、环化、臭氧化、Wittig羰基烯化、酯化、二醇化和硫化等 8步反应 ,合成了新型抗癌抗菌素“烯 -二”的双环前体 :6 -硫杂 - 13-氧杂双环[9.3.0 ]- 3,8-十四二 . 该合成路线步骤少 ,收率高 ,反应条件温和 .收藏指正
7.Under the following reaction conditions:access temperature of reactor was 30~35 ℃,LHSV was 1.5~2.0 h~ -1,pressure was 2.8 MPa,V(H_2)/V(C_9) was 400,the results of C_9 hydrogenated showed that m(Br_2)/m(C_9) reduced from 1.387 to 0.122~0.158.Under the following reaction conditions:temperature was 20~25 ℃,LHSV was 5.0 h~ -1,pressure was 1.3~1.5 MPa,n(H_2)/n(C_5) was 0.59,the results of C_5(the mass fraction of p- diolefin and alkyne was 35.0%~45.0%,olefin was 30.0%~40.0%) hydrogenated showed that the hydrogen fractional conversion of diolefin reached to 100% and the hydrogen fractional conversion of olefin reached to more than 95%.
结果表明:在反应器入口温度为30~35℃,空速为1.5~2.0h-1,反应压力为2.8MPa,V(H2)/V(C9)为400的工艺条件下加氢,可使裂解C9馏分的溴价[m(Br2)/m(C9馏分)]由1.387下降为0.122~0.158; 在反应器入口温度为20~25℃,总空速为5.0h-1,反应压力为1.3~1.5MPa,n(H2)/n(裂解C5)为0.59的工艺条件下,对双烯烃及炔烃质量分数为35.0%~45.0%且单烯烃质量分数为30.0%~40.0%的轻质C5馏分加氢,二烯烃加氢转化率可达100%,单烯烃加氢转化率为95%以上;收藏指正
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