International Transaction Journal of Engineering, Management, & Applied Sciences & Technologies


:: International Transaction Journal of Engineering, Management, & Applied Sciences & Technologies TuEngr+QR-Code

ISSN 2228-9860
eISSN 1906-9642


Vol.12(7) (2021)


  1. Osunlade F. N, Zhang J. Energy Efficient Control and Optimisation of Distillation Column Using Artificial Neural Network. Chem. Eng. Trans., 2014; 39:37- 42.
  2. Al-Mutairi E. M., Babaqi B. S. Energy Optimization of Integrated Atmospheric and Vacuum Crude Distillation Units in Oil Refinery with Light Crude. Asia-Pacific J Chem. Eng., 2014; 9:181-195.
  3. Robertson G, Palazoglu A. A multi-level simulation approach for the crude oil loading/unloading scheduling problem. Computers and Chemical Engineering, 2011; 35: 817-827.
  4. Osunlade F. N, Zhang, J. Energy Efficiency Optimisation for Distillation Column Using Artificial Neural Network Models. Energy, 2016; 106: 562-578.
  5. Li J, Misener R, Floudas C. A. Continuous-Time Modeling and Global Optimization Approach for Scheduling of Crude Oil Operations. AIChE J., 2012; 58: 205-226.
  6. Wang K, Zhang B.J, and Chen Q. L. Optimisation of a Crude Oil Distillation Unit based on Total Process Simulation, 26th European Symposium on Computer-Aided Process Engineering. Computer-Aided Chemical Engineering, 2016; 38: 2163-2168.
  7. Khalaf A. Steady-State Simulation of Basrah Crude Oil Refinery Distillation Unit using ASPEN HYSYS. Thi_Qar University Journal for Engineering Sciences, 2018; 9(2):29-39.
  8. Osuolale F. N, Zhanga Jie. Thermodynamic Optimization of Atmospheric Distillation Unit. Computers and Chemical Engineering, 2017;103: 201-209
  9. Yadav E. S, Indian T, Nayak D, Kumar C. A, and Selvakumar M. Simulation study of a distillation column using Aspen plus. Materials Today: Proceedings 2020.
  10. Bao J, Gao B, Wu X, Yoshimoto M, Nakao K. Simulation of industrial catalytic- distillation process for the production of methyl tert-butyl ether by developing user's model on aspen plus platform. Chem. Eng. J, 2002; 90(3):253-266.
  11. Abdulwahab G. Steady-state modeling of n-butyl acetate transesterification process using aspen plus: conventional versus integrated. ARPN J. Eng. Appl. Sci, 2012; 7(12): 1555-1564.
  12. Taqvi S.A, Tufa L.D, Muhadizir S. Optimization and dynamics of a distillation column using aspen plus. Procedia Eng., 2016; 148: 978-984.
  13. Luyben W.L. Aspen dynamics simulation of a middle-vessel batch distillation Process. J. Process Control, 2015; 33:49-59.
  14. Jalali A, Lotfi M and Mohammadi H. Simulation and energy integration of distillation tower of a naphtha treatment unit. Oil & Gas Science and Technology, 2018; 73:1-7.
  15. Aspen Tech. Aspen HYSYS Software, 2014.
  16. Basra Crude Oil Refinery, Research and Development Department. Refinery documents.
  17. KAMISLI F, AHMED A. Simulation and Optimization of a Crude Oil Distillation Unit. Turkish Journal of Science & Technology, 2019; 14(2): 59-68.
  18. Abolpour B, Abolpour R, Shamseddini A, Kamyabi S, and Hamzehee F. Optimization of the reflux ratio for the methanol-water stage distillation column. Research on Chemical Intermediates, 2013; 39:681-692.

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