气升式气-固环流汽提器的流体力学行为

刘梦溪; 卢春喜; 时铭显

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气升式气-固环流汽提器的流体力学行为

机译：气升式气-固环流汽提器的流体力学行为

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机译：In this paper, the principles of airlift loop reactor in gas-liquid and gas-liquid-solid systems are extended to gas-solid system. The models on bed average voidage in draft tube and the particle circulation velocity in a gas-solid loop reactor are deduced. The experiments are also conducted on a φ600mm×7000mm reactor. The catalyst voidage and catalyst circulation velocity are measured at different radial and axial positions in draft tube and annulus, respectively. The experimental data are analyzed systemically and represented satisfactorily by the proposed models.

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来源
《中国化学工程学报（英文版）》 |2004年第1期|55-59|共5页
作者
刘梦溪; 卢春喜; 时铭显;
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作者单位

Department of Chemical Engineering University of Petroleum Beijing 102249 China;

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收录信息中国科学引文数据库(CSCD);中国科技论文与引文数据库(CSTPCD);
原文格式 PDF
正文语种 chi
中图分类化学;
关键词
airlift loop reactors; bed average voidage; particle circulation velocity;
入库时间 2022-08-19 04:38:09

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气升式气-固环流汽提器的流体力学行为

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