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Process design Optimisation, heat integration, and techno-economic analysis of oil refinery: A case study

Jabbar, Khalaf J.; Zein, Sharif H.; Hasan, Abbas H.; Ahmed, Usama; Jalil, A. A.

Authors

Khalaf J. Jabbar

Profile image of Sharif Zein

Dr Sharif Zein S.H.Zein@hull.ac.uk
Senior Fellow HEA| Reader in Biorefinery Processes and Reaction Engineering| PI of Bioref Group

Usama Ahmed

A. A. Jalil



Abstract

This paper outlines a comprehensive analysis of the optimal design and simulation of a crude oil distillation system within a refinery process, including pre-treatment and blending of two crude oils to increase the refinery’s annual profit. This distillation process is currently in operation, and the desired amount of feedstock is obtained from Iraqi Basra light-2015 and Kirkuk-2011 crude oil. To improve the energy efficiency of the utilization rate of crude oil, an atmospheric distillation process unit in this refinery with a capacity of 150,000 barrels per day (bpd) is considered. Aspen HYSYS simulation is used to optimize the distillation unit configuration and its operating performance. This paper also deals with three scenarios by comparing the feedstock compositions to the distillation process and the produced product compositions to minimize utility consumption. A heat integration approach was applied to the 3rd scenario by recycling hot outlet streams to the heat exchangers to increase the temperature of the inlet stream of the distillation column. Results indicated that about £2.29 million per year (Mpy) could be saved from the heat integration systems. Economic analysis and cut yields were carried out for each scenario to investigate the cost-effective and economically viable. Based on the economic analysis, scenario three showed better performance with a comparatively high cumulative cash flow of £31,886 M.

Citation

Jabbar, K. J., Zein, S. H., Hasan, A. H., Ahmed, U., & Jalil, A. A. (2023). Process design Optimisation, heat integration, and techno-economic analysis of oil refinery: A case study. Energy Sources, Part A, 45(2), 4931-4947. https://doi.org/10.1080/15567036.2023.2205365

Journal Article Type Article
Acceptance Date Apr 11, 2023
Online Publication Date Apr 28, 2023
Publication Date Jan 1, 2023
Deposit Date Jul 7, 2023
Publicly Available Date Jul 11, 2023
Journal Energy Sources, Part A: Recovery, Utilization and Environmental Effects
Print ISSN 1556-7036
Electronic ISSN 1556-7230
Publisher Taylor & Francis
Peer Reviewed Peer Reviewed
Volume 45
Issue 2
Pages 4931-4947
DOI https://doi.org/10.1080/15567036.2023.2205365
Keywords Oil refinery, Design Optimization; Heat integration; Techno-economic analysis; Atmospheric distillation
Public URL https://hull-repository.worktribe.com/output/4298673

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Publisher Licence URL
http://creativecommons.org/licenses/by/4.0

Copyright Statement
© 2023 The Author(s). Published with license by Taylor & Francis Group, LLC.
This is an Open Access article distributed under the terms of the Creative Commons Attribution License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited. The terms on which this article has been published allow the posting of the Accepted Manuscript in a repository by the author(s) or with their consent.




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