Experimental investigation of fast-mode liquid modulation in a trickle-bed reactor

被引:28
作者
Banchero, M [1 ]
Manna, L [1 ]
Sicardi, S [1 ]
Ferri, A [1 ]
机构
[1] Politecn Torino, Dipartimento Sci Mat & Ingn Chim, I-10129 Turin, Italy
关键词
multiphase reactors; trickle-bed reactor; unsteady-state process; fast-mode operation; liquid modulation;
D O I
10.1016/j.ces.2004.03.048
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Unsteady-state operation of trickle-bed reactors (TBRs) is a promising technique to improve reactor performances especially when mass transfer phenomena are rate controlling. Among the different techniques, fast-mode modulation of the liquid flow rate seems to be one of the most successful. In fact cycling the liquid flow rate at very low frequencies can induce the reactor to work at the high-interaction regime where mass and heat transfer phenomena are strongly enhanced. Fast-mode periodic operation, then, can be considered an extension of the natural high-interaction regime at a mean range of gas and liquid flow rate normally associated with trickling regime in steady-state conditions. Experimental tests have been performed in a TBR employing alpha-methyl styrene hydrogenation on Pd/C catalyst in unsteady-state conditions by "on-off' fast-mode liquid modulation. Results have been compared with the steady-state experiments at the corresponding average liquid flow rate, revealing a conversion rate improvement up to 60%. All experiments have been performed in isothermal conditions, so conversion improvement can be ascribed only to mass transfer increase and not to thermal effects. The variation of gas and liquid flow rates and liquid cycle parameters presented several important implications about the optimal working conditions. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:4149 / 4154
页数:6
相关论文
共 15 条
[1]   Liquid-induced pulsing flow in trickle-bed reactors [J].
Boelhouwer, JG ;
Piepers, HW ;
Drinkenburg, AAH .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (16) :3387-3399
[2]   Enlargement of the pulsing flow regime by periodic operation of a trickle-bed reactor [J].
Boelhouwer, JG ;
Piepers, HW ;
Drinkenburg, AAH .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (20) :4661-4667
[3]   The induction of pulses in trickle-bed reactors by cycling the liquid feed [J].
Boelhouwer, JG ;
Piepers, HW ;
Drinkenburg, AAH .
CHEMICAL ENGINEERING SCIENCE, 2001, 56 (08) :2605-2614
[4]   EXPERIMENTAL-STUDY OF THE PERIODIC OPERATION OF A TRICKLE-BED REACTOR [J].
CASTELLARI, AT ;
HAURE, PM .
AICHE JOURNAL, 1995, 41 (06) :1593-1597
[5]   SOME LIQUID HOLDUP EXPERIMENTAL-DATA IN TRICKLE-BED REACTORS FOR FOAMING AND NONFOAMING HYDROCARBONS [J].
CHARPENTIER, JC ;
FAVIER, M .
AICHE JOURNAL, 1975, 21 (06) :1213-1218
[6]   Analysis of rate enhancement in a periodically operated trickle-bed reactor [J].
Gabarain, L ;
Castellari, AT ;
Cechini, J ;
Tobolski, A ;
Haure, P .
AICHE JOURNAL, 1997, 43 (01) :166-172
[7]   PERIODIC OPERATION OF A TRICKLE-BED REACTOR [J].
HAURE, PM ;
HUDGINS, RR ;
SILVESTON, PL .
AICHE JOURNAL, 1989, 35 (09) :1437-1444
[8]   Forced periodic operation of a trickle-bed reactor [J].
Lange, R ;
Gutsche, R ;
Hanika, J .
CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) :2569-2573
[9]   Investigations of periodically operated trickle-bed reactors [J].
Lange, R. ;
Hanika, J. ;
Stradiotto, D. ;
Hudgins, R. R. ;
Silveston, P. L. .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (24B) :5615-5621
[10]   EXPERIMENTAL-STUDY OF A TRICKLE-BED REACTOR OPERATING AT HIGH-PRESSURE - 2-PHASE PRESSURE-DROP AND LIQUID SATURATION [J].
LARACHI, F ;
LAURENT, A ;
MIDOUX, N ;
WILD, G .
CHEMICAL ENGINEERING SCIENCE, 1991, 46 (5-6) :1233-1246