Araştırma Makalesi
BibTex RIS Kaynak Göster

Development of a New Method to Optimize Operations of an Existing Crude Unit

Yıl 2024, , 52 - 61, 31.05.2024
https://doi.org/10.34088/kojose.1267986

Öz

A nonlinear optimization method working with the Simplex Method was developed to find optimum operating conditions of a crude oil distillation unit subject to defined process constraints, product specifications and prevailing market conditions. Then the method was applied to a commercial crude unit. This crude unit was modeled using Aspen Hysys V12.1 process simulation software. Two sets of market scenarios designated as the maximum gasoline scenario and minimum gasoline scenario were applied to the simulation model. It was found that the model minimized naphtha production and maximized kerosene production for minimum gasoline scenarios where the price of kerosene and diesel products were higher than naphtha products. Similarly, the model maximized the naphtha product yield for the maximum gasoline scenario where the naphtha price exceeds the mid-distillate product price. The iterative procedure developed for the study monotonically converged to optimum operating conditions for both market scenarios. It was observed that the optimization scheme developed in this study could generate a significant profit increase in the conventional crude unit investigated in this study without and capital investment.

Kaynakça

  • [1] Parkash, S., 2003, Refining Processes Handbook, Gulf Professional Publishing.
  • [2] Meyers, R. A., 1997 Handbook of Petroleum Refining Processes, 2nd ed., Mc-Graw Hill.
  • [3] Gary, J. H., Handwerk, G. E., Kaiser M. J., 2007, Petroleum Refining Technology and Economics, 5th ed., CRC Press.
  • [4] Fahim, M. A., Al-Sahhaf, T. A., Elkilani A. S., 2010, Fundamentals of Petroleum Refining, Elsevier, 1st ed.
  • [5] Steven, A. T., Pujado P. R., Jones D. S. J., 2015, Handbook of Petroleum Processing, Springer Reference, 2nd ed.
  • [6] Nelson, W. L., 1958, Petroleum Refinery Engineering, 4th ed., Mc.Graw Hill.
  • [7] Perry, R. H., Chilton C. H., Chemical Engineers’ Handbook, 5th ed., Mc-Graw Hill.
  • [8] Peters, M. S., Timmerhaus K. D., 1980, Plant Design and Economics for Chemical Engineers, 3rd ed., Mc-Graw Hill.
  • [9] Gürün Z., Bozdağ O., 2017, Enerji Santrallerinin Modellenmesi ve Optimizasyonu, Paper presented at 4. Enerji Verimliliği Konferansı, 13-14 October, Kocaeli, Turkey.
  • [10] Gürün Z., Bozdağ O., 2018, A Case Study on Modeling and Optimization of Power Plants, Paper presented at Petrochemical and Refining Conference Europe, April 9-10, Moskov, Russia.
  • [11] Gürün Z., Bozdağ O., 2019, Ham petrol Şarj Fırınlarında Optimizasyon, Paper presented at 22. Isı Bilimi ve Tekniği Kongresi, 11-14 September, Kocaeli, Turkey.
  • [12] Delewary A. R., 2018, Aspen Hysys ile Ham Petrol Damıtma Ünitesinin Simülasyonu, Masters Thesis, Kocaeli University.
  • [13]https://tprstaticfilessa.blob.core.windows.net/assets/uploads/yatirimcisunumlari/tr/yatirimci_sunumu_tem_%2023.pdf
  • [14] Kamışlı F., Ahmed A. A., 2019, Simulation and Optimization of A Crude Oil Distillation Unit, Turkish Journal of Science and Technology, 14(2), 59-68.
  • [15] Yang K., Liu S., He C., Zhang B., Chen Q., Pan M., 2020, Improving energy saving of crude oil distillation units with optimal operations, Journal of Cleaner Production, Vol 263, 121340
Yıl 2024, , 52 - 61, 31.05.2024
https://doi.org/10.34088/kojose.1267986

Öz

Kaynakça

  • [1] Parkash, S., 2003, Refining Processes Handbook, Gulf Professional Publishing.
  • [2] Meyers, R. A., 1997 Handbook of Petroleum Refining Processes, 2nd ed., Mc-Graw Hill.
  • [3] Gary, J. H., Handwerk, G. E., Kaiser M. J., 2007, Petroleum Refining Technology and Economics, 5th ed., CRC Press.
  • [4] Fahim, M. A., Al-Sahhaf, T. A., Elkilani A. S., 2010, Fundamentals of Petroleum Refining, Elsevier, 1st ed.
  • [5] Steven, A. T., Pujado P. R., Jones D. S. J., 2015, Handbook of Petroleum Processing, Springer Reference, 2nd ed.
  • [6] Nelson, W. L., 1958, Petroleum Refinery Engineering, 4th ed., Mc.Graw Hill.
  • [7] Perry, R. H., Chilton C. H., Chemical Engineers’ Handbook, 5th ed., Mc-Graw Hill.
  • [8] Peters, M. S., Timmerhaus K. D., 1980, Plant Design and Economics for Chemical Engineers, 3rd ed., Mc-Graw Hill.
  • [9] Gürün Z., Bozdağ O., 2017, Enerji Santrallerinin Modellenmesi ve Optimizasyonu, Paper presented at 4. Enerji Verimliliği Konferansı, 13-14 October, Kocaeli, Turkey.
  • [10] Gürün Z., Bozdağ O., 2018, A Case Study on Modeling and Optimization of Power Plants, Paper presented at Petrochemical and Refining Conference Europe, April 9-10, Moskov, Russia.
  • [11] Gürün Z., Bozdağ O., 2019, Ham petrol Şarj Fırınlarında Optimizasyon, Paper presented at 22. Isı Bilimi ve Tekniği Kongresi, 11-14 September, Kocaeli, Turkey.
  • [12] Delewary A. R., 2018, Aspen Hysys ile Ham Petrol Damıtma Ünitesinin Simülasyonu, Masters Thesis, Kocaeli University.
  • [13]https://tprstaticfilessa.blob.core.windows.net/assets/uploads/yatirimcisunumlari/tr/yatirimci_sunumu_tem_%2023.pdf
  • [14] Kamışlı F., Ahmed A. A., 2019, Simulation and Optimization of A Crude Oil Distillation Unit, Turkish Journal of Science and Technology, 14(2), 59-68.
  • [15] Yang K., Liu S., He C., Zhang B., Chen Q., Pan M., 2020, Improving energy saving of crude oil distillation units with optimal operations, Journal of Cleaner Production, Vol 263, 121340
Toplam 15 adet kaynakça vardır.

Ayrıntılar

Birincil Dil İngilizce
Konular Kimya Mühendisliği
Bölüm Makaleler
Yazarlar

Ziya Gürün 0000-0003-2971-3816

Osman Bozdağ Bu kişi benim 0000-0002-9734-6555

Erken Görünüm Tarihi 31 Mayıs 2024
Yayımlanma Tarihi 31 Mayıs 2024
Kabul Tarihi 23 Ekim 2023
Yayımlandığı Sayı Yıl 2024

Kaynak Göster

APA Gürün, Z., & Bozdağ, O. (2024). Development of a New Method to Optimize Operations of an Existing Crude Unit. Kocaeli Journal of Science and Engineering, 7(1), 52-61. https://doi.org/10.34088/kojose.1267986