Packing Size Effect on the Mean Bubble Diameter in a Fixed Bed under Gas–Liquid Concurrent Upflow-Reference-Cited by-同舟云学术

Packing Size Effect on the Mean Bubble Diameter in a Fixed Bed under Gas–Liquid Concurrent Upflow

Published:2017-04-27 Issue:45 Volume:56 Page:13490-13496
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Chen Zhaoxuan¹,Yang Jun¹,Ling Dan¹,Liu Peng¹,Ilankoon I. M. Saman K.²^ORCID,Huang Zibin¹,Cheng Zhenmin¹^ORCID

Affiliation:

1. State Key Laboratory of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China

2. Discipline of Chemical Engineering, School of Engineering, Monash University, Jalan Lagoon Selatan, 47500 Bandar Sunway, Selangor Darul Ehsan, Malaysia

Funder

National Natural Science Foundation of China

State Key Laboratory of Chemical Engineering of China

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.7b00123

Reference27 articles.

1. Pressure drop and flow regimes in cocurrent gas–liquid upflow through packed beds

2. Effect of solid characteristics on hydrodynamic and mass transfer in a fixed bed reactor operating in co-current gas–liquid up flow

3. Effect of a new high porosity packing on hydrodynamics and mass transfer in bubble columns

4. Effects of surface active agents on hydrodynamics and mass transfer characteristics in a split-cylinder airlift bioreactor with packed bed

5. Multi-scale analysis of the influence of physicochemical parameters on the hydrodynamic and gas–liquid mass transfer in gas/liquid/solid reactors

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