EFFECT OF VISCOSITY ON HYDRODYNAMIC PROPERTIES OF PULSING FLOW IN TRICKLE BEDS
Author:
Affiliation:
1. a Chemical Process Engineering Research Institute and Department of Chemical Engineering , Aristotle University ofThessaloniki , Univ. Box 455, Thessaloniki, GR 540 06, Greece
Publisher
Informa UK Limited
Subject
General Chemical Engineering,General Chemistry
Link
https://www.tandfonline.com/doi/pdf/10.1080/00986449808912384
Reference36 articles.
1. Residence time distribution in a liquid flowing cocurrently with a gas through a packed bed
2. Interfacial instabilities for horizontal gas-liquid flows in pipelines
3. Transition to pulsing flow, holdup and pressure drop in packed columns with cocurrent gas-liquid downflow
4. Hydrodynamics and mass transfer in three-phase cocurrent reactors
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1. Pressure drop and its reduction of gas–non-Newtonian liquid flow in downflow trickle bed reactor (DTBR);Chemical Engineering Research and Design;2014-01
2. Prediction of pulsation frequency of pulsing flow in trickle-bed reactors using artificial neural network;Chemical Engineering Science;2004-12
3. Hydrodynamics of Pulsing Flow in Three-Phase Fixed-Bed Reactor Operating at an Elevated Pressure;Industrial & Engineering Chemistry Research;2004-03-25
4. Hydrodynamics of the cocurrent downflow of a gas and a foaming liquid through a packed bed. Part I. Estimation of the transition boundary between the hydrodynamic regimes from the gas continuous flow to the pulsing flow;Chemical Engineering and Processing: Process Intensification;2004-02
5. Method for inferring contact angle and for correlating static liquid hold-up in packed beds;Chemical Engineering Science;2003-07
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