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cooling by making use of the system's exhaust gases. Ehyaei and Mozafari [54] performed energy, economic and environmental impact assessment of a micro gas turbine employed for on- site combined heat and power production, and examined the optimization of the micro turbine application to meet the electrical, heating and cooling loads of a building. Mago and Hueffed [18] evaluated a turbine driven combined cooling, heating and power (CCHP) system for large office buildings under various operating strategies, and explored the use of carbon credits to show how the possible reduction in carbon dioxide emissions via a CCHP system could translate into economic benefits. Ozgener et al. [55] developed an exergoeconomic model for a vertical ground source heat pump (GSHP) residential heating system. They calculated the ratio of thermodynamic loss rate to capital cost values to be in the range of 0.18 to 0.43, and provided a linear correlation between the value of this parameter and ambient temperatures. They also drew attention to the compressor as the component where the most exergy destruction occurred. Ozgener and Hepbasli [56] conducted an exergoeconomic analysis for a solar assisted ground source heat pump heating system with a 50 meter vertical and 32 millimeter nominal diameter U bend ground heat exchanger. They determined that the total exergy loss values were between 0.010 kW and 0.480 kW and found the largest energy and exergy losses in the greenhouse compressor. Moreover, they have calculated the ratio of thermodynamic loss rate to capital cost values to be in the range of 0.035 to 1.125. Many reports in the literature consider environmental aspects of thermal systems. Dincer [57] and Dincer and Rosen [47] considered the environmental and sustainability aspects of hydrogen and fuel cell systems. The exergetic and environmental aspects of drying systems have also been examined [17]. Ahmadi and Dincer [4] conducted an exergoenvironmental optimization of a CHP system using a genetic algorithm, and a sensitivity analysis of how optimized design parameters vary with the fuel cost. A thermodynamic analysis of post- combustion CO2 capture in a natural gas fired power plant has been reported by Amrolahi et al. [58]. Petrakopoulou et al. [59] studied exergoeconomic and exergoenvironmental analyses of a combined cycle power plant with chemical looping technology. This research provided an evaluation of chemical looping combustion technology from an economic and environmental perspective by comparing it with a reference plant, a combined cycle power plant that includes no CO2 capture. 42PDF Image | Energy Systems for Multigeneration Purposes
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