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Exergy and exergoeconomic analysis of a crude oil combined distillation unit

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  • Rivero, Ricardo
  • Rendón, Consuelo
  • Gallegos, Salvador

Abstract

The combined distillation unit is the first plant in a crude oil refinery, in which several intermediate products, i.e. liquid petroleum gas (LPG), naphtha, jet fuel, kerosene, diesel fuel, gas oils and reduced crude, are obtained through atmospheric and vacuum distillation of the crude oil mixture. It is important to determine the critical points in the unit from the exergy view point and to properly allocate the total production cost to the different simultaneously produced streams, to determine the monetary flows all through the plant, and to state the relevance in economic terms of the exergy losses of each individual equipment item. The results of the exergy and exergoeconomic analyses are presented in this paper. The most important factor affecting the transformation, operation and production costs of the products is the cost of the crude oil raw material; utilities, salaries, maintenance and even capital investment costs are less important. Also the critical points of the plant are presented which provide the basis for the optimization of the unit showing additional opportunities for process integration.

Suggested Citation

  • Rivero, Ricardo & Rendón, Consuelo & Gallegos, Salvador, 2004. "Exergy and exergoeconomic analysis of a crude oil combined distillation unit," Energy, Elsevier, vol. 29(12), pages 1909-1927.
    • Handle: RePEc:eee:energy:v:29:y:2004:i:12:p:1909-1927
    DOI: 10.1016/j.energy.2004.03.094
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    References listed on IDEAS

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    1. Tsatsaronis, Georgios & Winhold, Michael, 1985. "Exergoeconomic analysis and evaluation of energy-conversion plants—I. A new general methodology," Energy, Elsevier, vol. 10(1), pages 69-80.
    2. Tsatsaronis, Georgios & Winhold, Michael, 1985. "Exergoeconomic analysis and evaluation of energy-conversion plants—II. Analysis of a coal-fired steam power plant," Energy, Elsevier, vol. 10(1), pages 81-94.
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    Cited by:

    1. Gu, Wugen & Huang, Yuqing & Wang, Kan & Zhang, Bingjian & Chen, Qinglin & Hui, Chi-Wai, 2014. "Comparative analysis and evaluation of three crude oil vacuum distillation processes for process selection," Energy, Elsevier, vol. 76(C), pages 559-571.
    2. Haragovics, Máté & Mizsey, Péter, 2014. "A novel application of exergy analysis: Lean manufacturing tool to improve energy efficiency and flexibility of hydrocarbon processing," Energy, Elsevier, vol. 77(C), pages 382-390.
    3. Ghannadzadeh, Ali & Thery-Hetreux, Raphaële & Baudouin, Olivier & Baudet, Philippe & Floquet, Pascal & Joulia, Xavier, 2012. "General methodology for exergy balance in ProSimPlus® process simulator," Energy, Elsevier, vol. 44(1), pages 38-59.
    4. Mohammad Mehdi Parivazh & Milad Mousavi & Mansoor Naderi & Amir Rostami & Mahdieh Dibaj & Mohammad Akrami, 2022. "The Feasibility Study, Exergy, and Exergoeconomic Analyses of a Novel Flare Gas Recovery System," Sustainability, MDPI, vol. 14(15), pages 1-23, August.
    5. Claudia Toro & Matteo V. Rocco & Emanuela Colombo, 2016. "Exergy and Thermoeconomic Analyses of Central Receiver Concentrated Solar Plants Using Air as Heat Transfer Fluid," Energies, MDPI, vol. 9(11), pages 1-17, October.
    6. Silva, J.A.M. & Flórez-Orrego, D. & Oliveira, S., 2014. "An exergy based approach to determine production cost and CO2 allocation for petroleum derived fuels," Energy, Elsevier, vol. 67(C), pages 490-495.
    7. Silva, J.A.M. & Oliveira, S., 2014. "An exergy-based approach to determine production cost and CO2 allocation in refineries," Energy, Elsevier, vol. 67(C), pages 607-616.
    8. Raúl Arango-Miranda & Robert Hausler & Rabindranarth Romero-López & Mathias Glaus & Sara Patricia Ibarra-Zavaleta, 2018. "An Overview of Energy and Exergy Analysis to the Industrial Sector, a Contribution to Sustainability," Sustainability, MDPI, vol. 10(1), pages 1-19, January.
    9. Sadeghifar, Hamidreza & Safe Kordi, Ali Akbar, 2011. "A new and applicable method to calculate mass and heat transfer coefficients and efficiency of industrial distillation columns containing structured packings," Energy, Elsevier, vol. 36(3), pages 1415-1423.
    10. Charalampos Michalakakis & Jonathan M. Cullen, 2022. "Dynamic exergy analysis: From industrial data to exergy flows," Journal of Industrial Ecology, Yale University, vol. 26(1), pages 12-26, February.
    11. Oni, A.O. & Fadare, D.A. & Adeboye, L.A., 2017. "Thermoeconomic and environmental analyses of a dry process cement manufacturing in Nigeria," Energy, Elsevier, vol. 135(C), pages 128-137.
    12. Khalili-Garakani, Amirhossein & Ivakpour, Javad & Kasiri, Norollah, 2016. "Evolutionary synthesis of optimum light ends recovery unit with exergy analysis application," Applied Energy, Elsevier, vol. 168(C), pages 507-522.
    13. Fábrega, F.M. & Rossi, J.S. & d'Angelo, J.V.H., 2010. "Exergetic analysis of the refrigeration system in ethylene and propylene production process," Energy, Elsevier, vol. 35(3), pages 1224-1231.
    14. Wei, Zhiqiang & Zhang, Bingjian & Wu, Shengyuan & Chen, Qinglin & Tsatsaronis, George, 2012. "Energy-use analysis and evaluation of distillation systems through avoidable exergy destruction and investment costs," Energy, Elsevier, vol. 42(1), pages 424-433.
    15. Nur Izyan, Z. & Shuhaimi, M., 2014. "Exergy analysis for fuel reduction strategies in crude distillation unit," Energy, Elsevier, vol. 66(C), pages 891-897.

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