Design and operation of a radio-frequency heated micro-trickle bed reactor for consecutive catalytic reactions

被引:25
作者
Chatterjee, Sourav [1 ]
Degirmenci, Volkan [1 ]
Rebrov, Evgeny V. [1 ,2 ]
机构
[1] Queens Univ Belfast, Sch Chem & Chem Engn, Belfast BT9 5AG, Antrim, North Ireland
[2] Univ Warwick, Sch Engn, Coventry CV4 7AL, W Midlands, England
基金
欧洲研究理事会;
关键词
Micro trickle bed reactor; RF heating; Heat transfer; Consecutive reactions; CITRONELLAL; MENTHOL; (+/-)-CITRONELLAL; HYDROGENATION; MICROREACTOR; CYCLIZATION; STEP; BETA;
D O I
10.1016/j.cej.2015.06.096
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A radiofrequency heated micro-trickle bed reactor with two adjacent thermal zones was designed. In the first thermal zone, citronellal is converted to isopulegol over a H-ZSM-5 catalyst at 80 degrees C. This is followed by the second thermal zone where hydrogenation isopulegol to menthol occurs over a Pd/TiO2 catalyst at 70 degrees C. The two catalytic zones are separated by heating zones made of nickel ferrite particles that produce heat under radiofrequency field at 180 kHz. The position of the catalytic zones was determined based on a one dimensional heat transfer model, in which the actual flow pattern was approximated. Such configuration allows achieving desired temperatures in the catalyst beds whereas the inlet and outlet gas temperatures are close to ambient temperature which increases energy efficiency of the system. The overall product yield was increased by 9 times as compared with a single thermal zone configuration. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:884 / 891
页数:8
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