Liquid distribution in trickle-bed reactor

被引:55
作者
Marcandelli, C
Lamine, AS
Bernard, JR
Wild, G
机构
[1] ENSIC, CNRS, Lab Sci Genie Chim, F-54001 Nancy, France
[2] Univ Paris 13, CNRS, Lab Ingn Mat & Hautes Press, F-93430 Villetaneuse, France
[3] Elf Antar France, Ctr Rech Elf Solaize, F-69360 Solaize, France
来源
OIL & GAS SCIENCE AND TECHNOLOGY-REVUE D IFP ENERGIES NOUVELLES | 2000年 / 55卷 / 04期
关键词
trickle bed; liquid distribution; RTD (Residence-Time Distribution); liquid collector; pressure drop; tomography;
D O I
10.2516/ogst:2000029
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The aim of this study is to develop techniques to qualify the efficiency of liquid distribution in trickle-bed reactors, using cold mockups. The experimental setup consists mainly in a 0.3-m-ID packed-bed column with three different plates used to vary the quality of inlet hybrid distribution. Liquid distribution has been qualified using several techniques: global pressure drop measurements, global RTD (Residence-Time Distribution) of the liquid, local heat transfer probes, capacitance tomography, collector at the bottom of the reactor with nine equal zones. The bed pressure drop and the overall external liquid saturation decrease when the maldistribution increases; quantitative information is however difficult to obtain this way. Global RTD of the liquid allows quantifying of the average liquid distribution in the bed. The local thermal sensors given an indication of local liquid velocity and indicate possible local maldistribution of the liquid (scale mm) even when global distribution is good. Concerning the results obtained with the collector, a maldistribution index is defined, ranging from 0 (ideal distribution) to 1 (worst possible distribution), and the influence of the different operating parameters (gas and liquid velocities, particle shape) is discussed.
引用
收藏
页码:407 / 415
页数:9
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