Jump to ContentJump to Main Navigation
Show Summary Details
More options …

Chemical Product and Process Modeling

Ed. by Sotudeh-Gharebagh, Rhamat / Mostoufi, Navid / Chaouki, Jamal

4 Issues per year


CiteScore 2016: 0.94

SCImago Journal Rank (SJR) 2016: 0.270
Source Normalized Impact per Paper (SNIP) 2016: 0.928

Online
ISSN
1934-2659
See all formats and pricing
More options …

Fluid Catalytic Cracking Riser Modeling in Heat Transfer Mode

Raj Kumar Gupta / Vineet Kumar
Published Online: 2008-03-19 | DOI: https://doi.org/10.2202/1934-2659.1123

A 3-phase, one dimensional, heat transfer model for the fluid catalytic cracking riser reactor is developed. This model incorporates a new detailed kinetic model based on pseudo components' cracking. The model also includes the effect of local temperature on the reaction rate constants, variation of endothermic heat of cracking all along the riser height, and the heat of adsorption of the coke on the catalyst. Also, the developed model is compared with a 2-phase, one dimensional heat transfer model.The proposed model is capable of predicting the products' yields, phase temperatures, and phase velocities all along the riser height. Model predictions are very close to the data reported in literature.

Keywords: modeling and simulation; fluid catalytic cracking; riser kinetics; heat of cracking

About the article

Published Online: 2008-03-19


Citation Information: Chemical Product and Process Modeling, ISSN (Online) 1934-2659, DOI: https://doi.org/10.2202/1934-2659.1123.

Export Citation

©2011 Walter de Gruyter GmbH & Co. KG, Berlin/Boston. Copyright Clearance Center

Citing Articles

Here you can find all Crossref-listed publications in which this article is cited. If you would like to receive automatic email messages as soon as this article is cited in other publications, simply activate the “Citation Alert” on the top of this page.

[1]
Divyanshu Arya and Raj Kumar Gupta
Particulate Science and Technology, 2014, Volume 32, Number 2, Page 144

Comments (0)

Please log in or register to comment.
Log in