Influence of vertical heat exchanger tubes, their arrangement and the column diameter on the hydrodynamics in a gas–solid bubbling fluidized bed-Reference-Cited by-同舟云学术

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Influence of vertical heat exchanger tubes, their arrangement and the column diameter on the hydrodynamics in a gas–solid bubbling fluidized bed

Published:2017-12 Issue: Volume:97 Page:46-59
ISSN:0301-9322
Container-title:International Journal of Multiphase Flow
language:en
Short-container-title:International Journal of Multiphase Flow

Author:

Schillinger Frank,Maurer Simon,Wagner Evert C.,van Ommen J. Ruud,Mudde Robert F.,Schildhauer Tilman J.

Publisher

Elsevier BV

Subject

Fluid Flow and Transfer Processes,General Physics and Astronomy,Mechanical Engineering

Reference44 articles.

1. Experimental and computational study on the bubble behavior in a 3-D fluidized bed;Acosta-Iborra;Chem. Eng. Sci.,2011

2. Simultaneous algebraic reconstruction technique (SART): A superior implementation of the art algorithm;Andersen;Ultrason. Imaging,1984

3. Study of the effect of reactor scale on fluidization hydrodynamics using fine-grid {CFD} simulations based on the two-fluid model;Bakshi;Powder Technol.,2016

4. A study of pressure fluctuations in a bubbling fluidized bed;Baskakov;Powder Technol.,1986

5. The influence of the particle size distribution on fluidized bed hydrodynamics using high-throughput experimentation;Beetstra;AIChE J.,2009

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3. Non-invasive and non-intrusive diagnostic techniques for gas-solid fluidized beds – A review;Powder Technology;2024-01

4. X-ray imaging techniques for gas–solid fluidized beds: A technical review;Particuology;2023-11

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