Cyclodimerization of crotonaldehyde to form cyclohexadienecarbaldehydes and tolaldehydes over solid base catalysts

The cyclodimerization of crotonaldehyde was performed over acid or base catalysts in the gas phase. We first attempted the reaction over various acid and base catalysts using a pulse reactor. The typical bases, CaO and MgO, effectively promoted the reaction to form methylcyclohexadienecarbaldehydes...

Full description

Saved in:
Bibliographic Details
Published inReaction kinetics, mechanisms and catalysis Vol. 105; no. 2; pp. 401 - 412
Main Authors Kurokawa, Hideki, Yanai, Masashi, Ohshima, Masa-aki, Miura, Hiroshi
Format Journal Article
LanguageEnglish
Published Dordrecht Springer Netherlands 01.04.2012
Subjects
Online AccessGet full text

Cover

Loading…
More Information
Summary:The cyclodimerization of crotonaldehyde was performed over acid or base catalysts in the gas phase. We first attempted the reaction over various acid and base catalysts using a pulse reactor. The typical bases, CaO and MgO, effectively promoted the reaction to form methylcyclohexadienecarbaldehydes (MCHC) and tolaldehydes. In contrast, no significant formation of the dimers was observed over the acid catalysts, such as SiO 2 –Al 2 O 3 and H-mordenite. Aluminum oxide also promoted the dimerization, indicating that the dimerization proceeds on the weaker base sites. The main products in the formed dimers were 6-methylcyclohexa-1,3-dienecarbaldehyde and o -tolualdehyde. In addition, small amounts of 4-methylcyclohexa-1,5-dienecarbaldehyde and p -tolaldehyde were produced as dimers. When the dimerization was performed over CaO, MgO, and Al 2 O 3 using a fixed-bed flow reactor, the catalytic activities of all the catalysts significantly decreased during the initial stage of the reaction. The TG–DTA analysis of the used catalysts clearly indicated that a large amount of the condensation products had adsorbed on the catalyst surface. The maximum selectivity to the dimers (MCHC and tolaldehydes) was 38% for an approximate 30% conversion, which was obtained during the initial stage of the reaction over the Al 2 O 3 and CaO catalysts.
ISSN:1878-5190
1878-5204
DOI:10.1007/s11144-011-0381-5