Catalysts for Hydration of Cyclohexene to Cyclohexanol

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...

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Published inChemical research in Chinese universities Vol. 29; no. 4; pp. 743 - 746
Main Authors Fang, De-ren, Lu, Jin-yan, Zhang, Hui-min, Li, Jie, Wang, Yan-yan
Format Journal Article
LanguageEnglish
Published Berlin/Heidelberg Springer Berlin Heidelberg 01.08.2013
Shandong Provincial Key Lab of Chemical Engineering,Yantai University, Yantai 264005, P.R.China
Institute of Applied Catalysis,Yantai University, Yantai 264005, P.R.China%Shandong Provincial Key Lab of Chemical Engineering,Yantai University, Yantai 264005, P.R.China%Institute of Applied Catalysis,Yantai University, Yantai 264005, P.R.China
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Summary: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℃, the activity and selectivity of the modified resin ca- talyst 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 forma- tion of by-products.
Bibliography: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℃, the activity and selectivity of the modified resin ca- talyst 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 forma- tion of by-products.
Hydration; Cyclohexene; Ion-exchange resin; Modification; Aminate rate
22-1183/06
ISSN:1005-9040
2210-3171
DOI:10.1007/s40242-013-3091-x