Residence time, mass transfer and back-mixing of the liquid in trickle flow reactors containing porous particles

Iliuta I.; Larachi F.; Grandjean B.P.A.

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Residence time, mass transfer and back-mixing of the liquid in trickle flow reactors containing porous particles

机译：液体在包含多孔颗粒的滴流反应器中的停留时间，传质和返混

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来源
《Chemical Engineering Science》 |1999年第18期|共11页
作者
Iliuta I.; Larachi F.; Grandjean B.P.A.;
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原文格式 PDF
正文语种 eng
中图分类化学工业;
关键词
Trickle-bed reactor; Axial dispersion; Mass transfer;

机译：ckle流床反应器;轴向分散;传质;

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专利

1. Residence time, mass transfer and back-mixing of the liquid in trickle flow reactors containing porous particles [J] . Iliuta I., Larachi F., Grandjean B.P.A. Chemical Engineering Science . 1999,第18期

机译：液体在包含多孔颗粒的滴流反应器中的停留时间，传质和返混
2. Gas-liquid hydrogenation in continuous flow - The effect of mass transfer and residence time in powder packed-bed and catalyst-coated reactors [J] . Chemical engineering journal . 2020,第期

机译：连续流动的气液氢化 - 粉末填料床和催化剂涂覆的反应器中的传质和停留时间的作用
3. Cyclic variation of the liquid flow residence time in periodically operated trickle-bed reactors [J] . Borremans D, Rode S, Wild G Chemical Engineering Science . 2007,第26期

机译：周期性运行的滴流床反应器中液体流动停留时间的循环变化
4. EXPERIMENTAL EVIDENCE OF CORRELATION BETWEEN HYSTERESIS OF GAS-LIQUID MASS TRANSFER AND RADIAL LIQUID DISTRIBUTION IN A TRICKLE BED REACTOR [C] . R. Wang, M.-L. Luan, Z.-S.Mao, 1996 Asian-Pacific chemical reaction engineering forum(APCRE'96) . 1996

机译：RICK床反应器中气液传质迟滞与径向液体分布相关性的实验证据
5. Influence of Bed Depth on Specific Liquid-Solid Mass Transfer in a 5 m Trickle Bed Reactor [D] . Saayman, Francois. 2014

机译：床深对5 m ckle流床反应器中特定液固传质的影响
6. Strategic Application of Residence-Time Control in Continuous-Flow Reactors [O] . Dr. István M Mándity, Dr. Sándor B Ötvös, Prof. Dr. Ferenc Fülöp 2015

机译：停留时间控制在连续流反应器中的战略应用
7. Mass transfer between gas and particles in a gas-solid trickle flow reactor [O] . Kiel, J.H.A., Prins, W., van Swaaij, Willibrordus Petrus Maria 1992

机译：气固滴流反应器中气体与颗粒之间的传质

Residence time, mass transfer and back-mixing of the liquid in trickle flow reactors containing porous particles

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