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This paper presents the results of thermodynamic analysis of the crude distillation units of two refineries in Nigeria. The analysis was intended to assess the thermodynamic efficiencies of the refineries and proffer methods of improving the efficiencies. Presented results show the atmospheric distillation units of the refineries have 33.3% and 31.6% exergetic efficiencies and 86.5% and 74.6% energetic efficiencies, respectively. Modifications of the operating and feed conditions of the refineries resulted in increased exergetic efficiencies for as much as 62.3% and 38.7% for the refineries. Thermodynamic analysis of the refineries can bring about efficiency improvement and effectiveness of the refineries.
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Tom
Strony
83--102
Opis fizyczny
Bibliogr. 21 poz., rys., tab., wykr., wz.
Twórcy
- Department of Chemical Engineering, Ladoke Akintola University of Technology, P. M.B. 4000, Ogbomoso, Nigeria
autor
- Department of Chemical Engineering, Covenant University, Km. 10 Idiroko Road, P.M.B. 1023, Canaan Land, Ota, Ogun State, Nigeria
Bibliografia
- [1] Sankaranarayanan K., Arons J.D.S., Kooi, H.J.V.D.: Efficiency and Sustainability in the Energy and Chemical Industries. CRC Press, Taylor and Francis, 2010.
- [2] Fitzmorris R.E., Mah R.: Improving distillation column design using thermodynamic availability analysis. AICHE J. 6(1980), 2, 265–273.
- [3] Dincer I.: Energy and environmental impacts: present and future perspectives. Energ. Sources 20(1998), 427–453.
- [4] Stanek W., Budnik M.: Application of exergy analysis for evaluation of CO2 emission from operation of steam power unit. Arch. Thermodyn. 31(2010), 4, 81–91.
- [5] Sekret R., Nitkiewicz A.: Exergy analysis of the performance of low-temperature district heating system with geothermal heat pump. Arch. Thermodyn. 35(2014), 1, 77–86.
- [6] Budnik M., Stanek W.: Exergetic cost of a steam power plant operation. Arch. Thermodyn. 32(2011), 2, 39–54.
- [7] Dudar A., Butrymowicz D., Śmierciew K., Karwacki J.: Exergy analysis of operation of two-phase ejector in compression refrigeration systems. Arch. Thermodyn. 34(2013), 4, 107–122.
- [8] |sc Linnhoff B., Hindmarsh E.: The pinch design method of heat exchanger networks. Chem. Eng. Sci. 38(1983), 5, 745–760.
- [9] Linnhoff B., Dunford H., Smith R.: Heat integration of distillation column into overall processes. Chem. Eng. Sci. 38(1983), 8, 1175–1188.
- [10] Dincer I., Rosen M.A.: Exergy:energy, environment and sustainable development. Elsevier , Oxford 2012.
- [11] Anozie A.N., Osuolale F.N., Aseeperi T.C.: Exergy analysis and optimization of binary plate distillation column operations. Int. J. Exergy 7(2010), 5, 593–606.
- [12] Anozie A.N, Osuolale F.N., Osunleke A.S.: Exergy analysis of binary plate distillation column operations. Int. J. Exergy 6(2009), 5, 715–728.
- [13] Szargut J., Morris D.R., Steward F.R.: Exergy Analysis of Thermal, Chemical and Metallurgical Processes. Hemisphere, New York 1988.
- [14] Rivero R., Rendón C., Monroy L.: The exergy of crude oil mixtures and petroleum fractions: calculation and application. Int. J. Appl. Thermodyn. 2(1999), 3, 115–123.
- [15] Al-Muslim H., Dincer I.: Thermodynamic analysis of crude oil distillation Systems. Int. J. Energy Res. 29(2005), 637–653.
- [16] Cornelissen R.L.: Thermodynamics and sustainable development, the use of exergy analysis and the reduction of irreversibility. PhD thesis, University of Twente, Enschede 1997, http://www.ub.utwente.nl.webdocs/wb/1/t0000003.pdf (assesed 5 March 2007).
- [17] Sea J.W., Oh M., Lee T.H.: Design optimization of a crude oil distillation. Chem. Eng. Technol. 23(2000), 2, 157–164.
- [18] Agrawal R., Herron D.M.: Optimal thermodynamic feed conditions for distillation of ideal binary mixtures. AIChE J., 43(1997), 11, 2984–2996.
- [19] Soave G., Feliu J.A.: Saving energy in distillation towers by feed splitting. Appl. Therm. Eng. 22(2002), 889–896.
- [20] Bandyopadhyay S.: Effect of feed on optimal thermodynamic performance of a distillation column. Chem. Eng. J. 88(2002), 1-3, 175–186.
- [21] HYSYS (2003) Version 3.2 (Build 5029), aspen Technology Inc., Licensed to TEAM LND, Calgary, Alberta, Canada
Uwagi
PL
Opracowanie rekordu w ramach umowy 509/P-DUN/2018 ze środków MNiSW przeznaczonych na działalność upowszechniającą naukę (2019).
Typ dokumentu
Bibliografia
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bwmeta1.element.baztech-caac3f6c-e0e1-46a3-a337-1ca5828a7757