Gas–liquid simulation of an airlift bubble column reactor-Reference-Cited by-同舟云学术

Gas–liquid simulation of an airlift bubble column reactor

Published:2004-02 Issue:2 Volume:43 Page:137-144
ISSN:0255-2701
Container-title:Chemical Engineering and Processing: Process Intensification
language:en
Short-container-title:Chemical Engineering and Processing: Process Intensification

Author:

Blažej M.,Cartland Glover G.M.,Generalis S.C.,Markoš J.

Publisher

Elsevier BV

Subject

Industrial and Manufacturing Engineering,Process Chemistry and Technology,Energy Engineering and Power Technology,General Chemical Engineering,General Chemistry

Reference15 articles.

1. Fluent Solvers, Fluent Europe Ltd, Sheffield Airport Business Park, Europa Link, Sheffield S9 1XU (http://www.fluent.co.uk).

2. Application of a magnetic tracer method for the characterisation of hydrodynamics in internal-loop airlift bioreactors;Klein;Chem. Pap.,2000

3. CFD and bubble column reactors: simulation and experiment;Cartland Glover;Chem. Pap.,2000

4. G.M. Cartland Glover, S.C. Generalis, N.H. Thomas, Dynamic simulations of multiphase flow in bubble columns, Chisa 2000, Poster G5.5, Prague, Czech Republic, 27–31 August 2000.

5. Airlift Bioreactors;Chisti,1989

Cited by 46 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. CFD analysis of multiphase flow in an airlift reactor: superficial velocity and gas holdup influence on the loop recirculation;Brazilian Journal of Chemical Engineering;2024-07-26

2. Hydrodynamics and mass transfer of concentric-tube internal loop airlift reactors: A review;Bioresource Technology;2022-09

3. Prediction of gas holdup in various types of airlift reactors;Korean Journal of Chemical Engineering;2021-08-05

4. Advances in characteristics analysis, measurement methods and modelling of flow dynamics in airlift reactors;Chemical Engineering and Processing - Process Intensification;2019-10

5. Performance of an integrated reactor with airlift loop and sedimentation for municipal wastewater treatment: A 150 m 3 /d pilot case study;The Canadian Journal of Chemical Engineering;2019-09-25