Optimal Design of Petroleum Refinery Configuration Using a Model-Based Mixed-Integer Programming Approach with Practical Approximation-Reference-Cited by-同舟云学术

Optimal Design of Petroleum Refinery Configuration Using a Model-Based Mixed-Integer Programming Approach with Practical Approximation

Published:2018-05-16 Issue:22 Volume:57 Page:7555-7565
ISSN:0888-5885
Container-title:Industrial & Engineering Chemistry Research
language:en
Short-container-title:Ind. Eng. Chem. Res.

Author:

Albahri Tareq A.¹,Khor Cheng Seong²³^ORCID,Elsholkami Mohamed⁴,Elkamel Ali⁴⁵^ORCID

Affiliation:

1. Chemical Engineering Department, Kuwait University, P.O. Box 5969, Safat 13060, Kuwait

2. Chemical Engineering Department, Universiti Teknologi PETRONAS, 32610 Seri Iskandar, Perak Darul Ridzuan, Malaysia

3. Chemical Engineering Programme, Xiamen University Malaysia, Jalan Sunsuria, Bandar Sunsuria, 43900 Sepang, Selangor Darul Ehsan, Malaysia

4. Department of Chemical Engineering, University of Waterloo, Waterloo, ON N2L 3G1, Canada

5. Department of Chemical Engineering, Khalifa University, The Petroleum Institute, Abu Dhabi 2533, United Arab Emirates

Publisher

American Chemical Society (ACS)

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.iecr.7b04507

Reference55 articles.

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2. Bonilla, J. A. Delayed Coking and Solvent Deasphalting: Options for Residue Upgrading. Presented at the AIChE Annual Meeting, Anaheim, CA, 1982.

3. Integration of hierarchical decomposition and mathematical programming for the synthesis of process flowsheets

4. A superstructure optimization approach for water network synthesis with membrane separation-based regenerators

5. A Superstructure Optimization Approach for Membrane Separation-Based Water Regeneration Network Synthesis with Detailed Nonlinear Mechanistic Reverse Osmosis Model

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