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the choice between the three options for LNG evaporation. 6. Future Research In the future, a more detailed investigation and analysis will be carried out of options for the evaporation of LNG. LNG is one of the case studies in a more general research after the consequences of involving exergy analysis in decisions regarding future energy supply with respect to the environmental, economical and social aspects of the sustainability of this energy supply. Nomenclature Ex exergy flow, J/s H enthalpy, J/mol . m mass flow rate, kg/s Q heat flow rate, J/s S entropy, J/(mol K) T temperature [K] W work, J/s Subscripts and superscripts 0 at reference conditions (1 bar, 10 °C) max theoretical amount ph physical References [1] Dincer, I. and Rosen, M., 2007, Exergy: energy, environment and sustainable develop- ment, Elsevier, Oxford, UK. [2] Zagoruchenko, V. and Zhuravlev, A., 1970, Thermophysical properties of gaseous and liquid methane, Israel Program for Scientific Translations Ltd, Jerusalem. [3] Tarakad, R.R., 2003, LNG receiving and regasification terminals, Revised edition, Zeus Development Corporation, Houston. [4] Sugiyama, M., The Utilization of LNG Cryogenic Energy, Energy and Information Technology Journal [online journal], EIT No. 32, URL: http://www.eit.or.jp/magazine/pdf/ eit32e.pdf. [5] Tsatsaronis, G. and Morosuk, T., 2010, Advanced exergetic analysis of a novel system for generating electricity and vaporizing liquefied natural gas, Energy, 35(2), pp. 820-829. [6] Szargut, J. and Szczygiel, I., 2009, Utilization of the cryogenic exergy of liquid natural gas (LNG) for the production of electricity, Energy, 34(7), pp. 827-837. [7] Liu, M., et al., 2009, Thermoeconomic analysis of a novel zero-CO2-emission high- efficiency power cycle using LNG coldness, Energy Conversion and Management, 50(11), pp. 2768-2781. [8] Lu, T. and Wang, K., 2009, Analysis and optimization of a cascading power cycle with liquefied natural gas (LNG) cold energy recovery, Applied Thermal Engineering, 29(8- 9), pp. 1478-1484. [9] Deng, S., et al., 2004, Novel cogeneration power system with liquefied natural gas (LNG) cryogenic exergy utilization, Energy, 29(4), pp. 497-512. [10]Buck, A. de, Croezen, H. and Rensma, K., 2008, The ‘oxy-fuel’ route (in Dutch), Technical Report, 08.3509.09, CE, Delft, The Netherlands. [11]Anonymous, 2008, The LNG/oxyfuel route for new coal plants – Environmental benefits plus cost savings?, Brochure, 2MJAF0801, SenterNovem, Utrecht, The Netherlands. [12] Anonymous, 2004, LNG vaporizer options study for ConocoPhillips, Technical Report, Exhibit G, Foster Wheeler USA Corp., USA. [13]Coulson, J.M. and Richardson, J.F., 1983, An Introduction to Chemical Engineering Design, 1st ed., Pergamon Press, Oxford, UK. [14]Anonymous, 2006, DACE price booklet, 25th ed., Reed Business Information bv, Doetinchem, The Netherlands. In: D. Favrat & F. Maréchal (eds.), ECOS2010: Proceedings of the 23rd International Conference on Efficiency, Cost, Optimization, Simulation, and Environmental Impact of Energy Systems, 14 – 17 June 2010, Lausanne, Switzerland, Volume II, pp. 441-446.PDF Image | Exergy Efficient Application of LNG Cold
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