Catalysts for hydration of cyclohexene to cyclohexanol

De-ren Fang , Jin-yan Lu , Hui-min Zhang , Jie Li , Yan-yan Wang

Chemical Research in Chinese Universities ›› 2013, Vol. 29 ›› Issue (4) : 743 -746.

PDF
Chemical Research in Chinese Universities ›› 2013, Vol. 29 ›› Issue (4) : 743 -746. DOI: 10.1007/s40242-013-3091-x
Article

Catalysts for hydration of cyclohexene to cyclohexanol

Author information +
History +
PDF

Abstract

The hydration of cyclohexene was determined in a stirred tank of 100 mL in a batch mode in the presence of modified or unmodified resin as catalyst. The ion-exchange sulfonate resin was modified with alkyl secondary amine. At an optimum amination rate of 15%, the conversion of cyclohexene reached to 22% and the selectivity of cyclohexanol was 95.6%. In a temperature range of 90–150 °C, the activity and selectivity of the modified resin catalyst were much higher than those of the unmodified resin catalyst, which was attributed to the inclusion formed between cyclohexene and alkyl chain and also the quasi-lipophilic phase formed around the outer surface of resin beads. The formed quasi-lipophilic phase formed enhanced the conversion of cyclohexene and depressed the formation of by-products.

Keywords

Hydration / Cyclohexene / Ion-exchange resin / Modification / Aminate rate

Cite this article

Download citation ▾
De-ren Fang, Jin-yan Lu, Hui-min Zhang, Jie Li, Yan-yan Wang. Catalysts for hydration of cyclohexene to cyclohexanol. Chemical Research in Chinese Universities, 2013, 29(4): 743-746 DOI:10.1007/s40242-013-3091-x

登录浏览全文

4963

注册一个新账户 忘记密码

References

[1]

Ishida H. Catal. Surv. Jpn., 1997, 1: 241.

[2]

Ishida H. Petrotech., 1996, 19: 1030.

[3]

Wang D Z, Shu X T, He M Y. Chin. J. Catal., 2002, 23: 503.

[4]

Shen W, Lin Q X, Zhu M Q. China Synth. Fiber Ind., 2009, 2: 45.

[5]

Mitsui O., Fukuoka Y., Process for Producing Cyclic Alcohol, US4588846, 1986

[6]

Kralik M, Hromec M, Kucem M. Petroleum and Coal, 1995, 37: 60.

[7]

Yang F, Chen G W, Li H Q, Guo X W, Wang X S. Chin. J. Catal., 2006, 27: 459.

[8]

Ma B L, Chun Y, Zhou W, Pan J, Xu Q H, Dong J L. Chem. J. Chinese Universities, 2005, 26(4): 731.

[9]

Wang M M, Yao Z L, Zhao R S. Ind. Catal., 2011, 2: 40.

[10]

Shan X L, Cheng Z M. Chem. React. Eng. Tech., 2008, 3: 252.

[11]

Frank S, Kai S. Ind. Eng. Chem. Res., 2008, 47: 9581.

[12]

Amit K, Kai S. Ind. Eng. Chem. Res., 2009, 48: 9534.

[13]

Zhang H, Mahajani S M, Sharma M M, Sridhar T. Chem. Eng. Sci., 2002, 57: 315.

[14]

Panneman H J, Beenackers A A C M. Ind. Eng. Chem. Res., 1992, 31: 1425.

[15]

Fang D R, Ren W Z, Lv H Y, Yang H T. J. Nat. Gas Chem., 2012, 21: 314.

[16]

Thorton R, Gates B C. J. Catal., 1974, 34: 275.

[17]

Wu J M, Dai X M, Chen J L, Guo W D. Chem. Ind. Eng. Progr., 2003, 22: 1222.

[18]

Frilette V J, Mower E B, Rubin M K. J. Catal., 1964, 3: 25.

AI Summary AI Mindmap
PDF

175

Accesses

0

Citation

Detail

Sections
Recommended

AI思维导图

/