[1]Ghazizahedi, A., “Simulation and retrofit Design of Isomerization Process”, Ph.D. Dissertation (Supervisor: Dr. Majid Hayati-Ashtiani), University of Kashan, in Persian, (2021).
[2] Martín, Á., Mato, F. A., "Hint: An Educational Software for Heat Exchanger Network Design with the Pinch Method",. Education of Chemical Engineering, Vol. 3, pp. 6-14, (2008).
[3] Mehdizadeh-Fard, M., Pourfayaz, F., Kasaeian, A. B., "Mehrpooya, M., A Practical Approach to Heat Exchanger Network Design in a Complex Natural Gas Refinery", Journal of Natural Gas Science and Engineering, Vol. 40, pp. 141-177, (2017).
[4] Feng, X., Pu, J., Yang, J., Chu, K. H., "Energy Recovery in Petrochemical Complexes through Heat Integration Retrofit Analysis", Applied Energy, Vol. 88, pp. 1965-1982, (2011).
[5] Szklo, A., Schaeffer, R., :Fuel Specification, Energy Consumption and CO2 Emission in Oil Refineries", Energy, Vol. 32, pp. 1075-1092, (2007).
[6] Jarullah, A. T., Abed, F. M., Ahmed, A. M., Mujtaba, L. M., "Optimisation of Several Industrial and Recently Developed AJAM Naphtha Isomerization Processes Using Model Based Techniques", Computers and Chemical Engineering, Vol. 126, pp. 403-420, (2019).
[7] Jarullah, A. T., Abed, F. M., Al-Tabbakh, B. A., Mujtaba, I. M., "Optimisation of several industrial and recently developed AJAM naphtha isomerization processes using model based techniques", Computer & Chemical Engineering, Vol. 126, pp. 403-420 (2019).
[8] Ghazizahedi, Z., Hayati-Ashtiani, M., "Retrofitting isomerization process to increase gasoline quality and decrease CO2 emission along with energy analysis using Pinch Technology", Energy Sources, Part A: Recovery, Utilization and Environmental Effects, (2020). DOI: 10.1080/15567036.2020.1859008
[9] Mohamed, M. F., Shehata, W. M., Abdel Halim, A. A., Gad, F. K., "Improving Gasoline Quality Produced from MIDOR Light Naphtha Isomerization Unit", Egyptian Journal of Petroleum, Vol. 26, pp. 111-124 (2017).
[10] Chekantsev, N. V., Gyngazova, M. S., Ivanchina E. D., "Development of Complex Mathematical Model of Light Naphtha Isomerization and Rectification Processes", Chemical Engineering Journal, Vol. 238, pp. 120-129, (2014).
[11] Dhar, A., Vekariya, R. L., Sharma, P., "Kinetics and Mechanistic Study of n-Alkane Hydroisomerization reaction on Pt-doped γ-alumina catalyst", Petroleum, Vol. 3, pp. 489-495, (2017).
[12] Ebrahim, M., Kawari, A., "Pinch Technology: an Efficient Tool for Chemical-plant Energy and Capital-cost Saving", Applied Energy, Vol. 65, pp. 45-49, (2000).
[13] Kang, H., Wang, T., Zheng, H., "Comparative Analysis of Regenerative and Air-extraction Multi-stage Humidification–dehumidification Desalination System Using Pinch Technology", Desalination, Vol. 385. pp. 158-166, (2016).
[14] Manan, Z. A., Nawi, W. N. R. M., Alwi, Sh. R. W., Klemes, J. J., "Advances in Process Integration Research for CO2 Emission Reduction–A Review", Journal of Clean Production, Vol. 167, pp. 1-13, (2017).
[15] Gu, K., Vassiliadis, V. S., "Limitations in Using Euler's Formula in the Design of Heat Exchanger Networks with Pinch Technology", Computers and Chemical Engineering, Vol. 68, pp. 123-127, (2014). DOI: 10.1080/15567036.2020.1859008