TY - JOUR
T1 - Synthesis and isomerization of chlorinated isopentene
AU - Cao, Ya
AU - Cui, Mifen
AU - Chen, Xian
AU - Fei, Zhaoyang
AU - Tang, Jihai
AU - Qiao, Xu
N1 - Publisher Copyright:
©, 2015, Zhejiang University. All right reserved.
PY - 2014/12/25
Y1 - 2014/12/25
N2 - 1-chloroisopentene was synthesized with isoprene and hydrogen chloride as raw materials in a three-phase bubbling reactor. The influence of the flow of hydrogen chloride, the reactive depth of isoprene and purging with N2 at different time intervals after stopping loading hydrogen chloride on the conversion of isoprene and the yield of 1-chloroisopenteneand dichlorohydrins isopentane was investigated. The results showed that the appropriate reaction conditions were 85 g isoprene, 1 g cuprous chloride and 1 g acetate acid, at 320 mL/min hydrogen chloride for 1.5 h, when residual quantity of isoprene being 3%-5%(mass fraction) stopping hydrogen chloride and purging with N2 at 120 mL/min for 1 h at 15-20℃, the conversion of isoprene and the yield of 1-chloroisopentene reached 96%-98% and 83%-85%, respectively. The equilibrium time and composition which the isomerization reached equilibrium were obtained. The equilibrium constant of 3-chloroisopentene to 1-chloroisopentene reached 9.21 at 0℃. The reaction heat of the isomerization was -9.64 kJ/mol, and low temperature was favorable for 3-chloroisopentene to 1-chloroisopentene.
AB - 1-chloroisopentene was synthesized with isoprene and hydrogen chloride as raw materials in a three-phase bubbling reactor. The influence of the flow of hydrogen chloride, the reactive depth of isoprene and purging with N2 at different time intervals after stopping loading hydrogen chloride on the conversion of isoprene and the yield of 1-chloroisopenteneand dichlorohydrins isopentane was investigated. The results showed that the appropriate reaction conditions were 85 g isoprene, 1 g cuprous chloride and 1 g acetate acid, at 320 mL/min hydrogen chloride for 1.5 h, when residual quantity of isoprene being 3%-5%(mass fraction) stopping hydrogen chloride and purging with N2 at 120 mL/min for 1 h at 15-20℃, the conversion of isoprene and the yield of 1-chloroisopentene reached 96%-98% and 83%-85%, respectively. The equilibrium time and composition which the isomerization reached equilibrium were obtained. The equilibrium constant of 3-chloroisopentene to 1-chloroisopentene reached 9.21 at 0℃. The reaction heat of the isomerization was -9.64 kJ/mol, and low temperature was favorable for 3-chloroisopentene to 1-chloroisopentene.
KW - Bubbling reactor
KW - Chlorinated isopentene
KW - Dichlorinatedisopentane
KW - Isomerization
UR - http://www.scopus.com/inward/record.url?scp=84921871139&partnerID=8YFLogxK
M3 - 文章
AN - SCOPUS:84921871139
SN - 1001-7631
VL - 30
SP - 544
EP - 549
JO - Huaxue Fanying Gongcheng Yu Gongyi/Chemical Reaction Engineering and Technology
JF - Huaxue Fanying Gongcheng Yu Gongyi/Chemical Reaction Engineering and Technology
IS - 6
ER -