Efficient Use of Energy through Incorporation of a Gas Turbine in Methanol Plant

Autor: M. Azadi, N. Tahouni, M. H. Panjeshahi
Jazyk: angličtina
Rok vydání: 2014
Předmět:
DOI: 10.5281/zenodo.1094785
Popis: A techno-economic evaluation for efficient use of energy in a large scale industrial plant of methanol is carried out. This assessment is based on integration of a gas turbine with an existing plant of methanol in which the outlet gas products of exothermic reactor is expanded to power generation. Also, it is decided that methanol production rate is constant through addition of power generation system to the existing methanol plant. Having incorporated a gas turbine with the existing plant, the economic results showed total investment of MUSD 16.9, energy saving of 3.6 MUSD/yr with payback period of approximately 4.7 years.
{"references":["Narvaez, D. Chadwick, L. Kershenbaum, \"Small-medium scale\npolygeneration systems: Methanol and power Production\" Applied\nEnergy, 2014. 113: p. 1109–1117.","M. Soltanieh, K.M. Azar, and M. Saber, \"Development of a zero\nemission integrated system for co-production of electricity and methanol\nthrough renewable hydrogen and CO2 capture\"International Journal of\nGreenhouse Gas Control, 2012. 7(0): p. 145-152.","A.K. Kralj,\"Electricity cogeneration in an exothermic reactor circuit\nsystem using an open gas turbine\" Fuel, 2014. 118(0): p. 220-226.","M. Sahafzadeh, A. Ataei, N. Tahouni, M.H. Panjeshahi, \"Integration of a\ngas turbine with an ammonia process for improving energy efficiency\"\nAppl. Therm. Eng. 58 (2013) 594-604.","H. Axelsson, S. Harvey, A. Asblad, T. Berntsson, \"Potential for\ngreenhouse gas reduction in industry through increased heat recovery\nand/or integration of combined heat and power\" Appl. Therm. Eng. 23\n(2003) 65–87.","B. Kalitventzeff, F. Mare´chal, H. Closon, \"Better solutions for process\nsustainability through better insight in process energy integration\" Appl.\nTherm. Eng. 21 (2001) 1349–1368.","F.J.J.G Janssen, A.H.M. Verkooijen, P.J. Ploumen, \"Synthesis of\nethane\" European Patent 0753652, assigned to N.V. Kema, The\nNetherlands, 1997.","M.A. Agee, L.J. Weick, K.L. Agee, E.L. Trepper, \"Synthesis gas\nproduction system and method\"US Patent 6155039, assigned to\nSyntroleum Corp (US), 2000.","J. Perold, I.L. Greeff, K.J. Ptasinski, F.J.J.G Janssen, \"Using a turbine\nexpander to recover exothermic reaction heat a case study on a phthalic\nanhydride process\" S. Afr. J. Chem. 13(2001) 1–14.\n[10] I.L. Greeff, J.A. Visser, K.J. Ptasinski, F.J.J.G Janssen, \"Utilization of\nreactor heat in methanol synthesis to reduce compressor duty application\nof power cycle principles and simulation tools\" Appl. Therm. Eng. 22\n(2002)1549–1458.\n[11] I.L. Greeff, J.A. Visser, K.J. Ptasinski, F.J.J.G. Janssen, \"Integration of a\nturbine expander with an exothermic reactor loopdflow sheet\ndevelopment and application to ammonia production\" Energy. 28 (2003)\n1495-1509.\n[12] A. K. Kralj , P. Glavic, \"Multi-criteria optimization in a methanol\nprocess\" Appl. Therm. Eng. 29 (2009) 1043–1049.\n[13] H.P. Loh, J. Lyons, I. Charles, W. White, \"Process Equipment Cost\nEstimation\" Final report, U.S. Department of Energy, National Energy\nTechnology Laboratory, 2002. DOE/NETL-2002/1169.\n[14] BahadorBakhtiari, Serge Bedard, \"Retrofitting heat exchanger networks\nusing a modified network pinch approach\"Applied Thermal\nEngineering, Volume 51, Issues 1–2, March 2013, Pages 973-979.\n[15] Kheen Nam Sun, SharifahRafidah Wan Alwi, Zainuddin Abdul Manan,\n\"Heat exchanger network cost optimization considering multiple utilities\nand different types of heat exchangers\" Computers & Chemical\nEngineering, Volume 49, 11 February 2013, Pages 194-204."]}
Databáze: OpenAIRE