Fluidized bed hydrodynamic modeling of CO 2 in syngas: Distorted RTD curves due to adsorption on FCC-Reference-Cited by-同舟云学术

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Fluidized bed hydrodynamic modeling of CO 2 in syngas: Distorted RTD curves due to adsorption on FCC

Published:2021-08-10 Issue:11 Volume:67 Page:
ISSN:0001-1541
Container-title:AIChE Journal
language:en
Short-container-title:AIChE J

Author:

Bérard Ariane¹^ORCID,Blais Bruno¹^ORCID,Patience Gregory S.¹^ORCID

Affiliation:

1. Department of Chemical Engineering Polytechnique Montréal Montreal Quebec Canada

Funder

Canada Foundation for Innovation

Natural Sciences and Engineering Research Council of Canada

Publisher

Wiley

Subject

General Chemical Engineering,Environmental Engineering,Biotechnology

Link

https://onlinelibrary.wiley.com/doi/pdf/10.1002/aic.17380

Reference33 articles.

1. Experimental methods in chemical engineering: Residence time distribution—RTD

2. Effect of tracer material properties on the residence time distribution (RTD) of continuous powder blending operations. Part I of II: Experimental evaluation

3. Study of fluid dynamic conditions in the selected static mixers part II-determination of the residence time distribution

4. Residence time distribution in rapid multiphase reactors

5. Particle velocities and their residence time distribution in the riser of a CFB

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2. Fluidisation behaviour and wall effects of cohesive hydrotalcite powder in a micro-fluidised bed;Powder Technology;2023-02

3. Application of general unit hydrograph model for marathon finish time distributions;Physica A: Statistical Mechanics and its Applications;2022-12

4. Fluidized‐bed reactor scale‐up : Reaction kinetics required;AIChE Journal;2022-06-25

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