2018
DOI: 10.1016/j.geothermics.2017.08.011
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Energy, exergy and exergoeconomic analysis of a cogeneration system for power and hydrogen production purpose based on TRR method and using low grade geothermal source

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Cited by 104 publications
(15 citation statements)
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“…In Equation (11), f k is the exergoeconomic factor. Also, the product cost rate is obtained from the exergoeconomic perspective for the whole process from the Equation (14).…”
Section: Exergoeconomic Analysismentioning
confidence: 99%
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“…In Equation (11), f k is the exergoeconomic factor. Also, the product cost rate is obtained from the exergoeconomic perspective for the whole process from the Equation (14).…”
Section: Exergoeconomic Analysismentioning
confidence: 99%
“…Figure 2 provides an illustration of the performance of multi-objective evolutionary algorithms. 26 In this optimization it is attempted to have the lowest cost rate parameter of the whole process, obtained from Equation (14), and also to achieve the highest efficiency of this process.…”
Section: Optimizationmentioning
confidence: 99%
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“…Ghaebi et al 118 modified an ORC with a regenerative using different working fluids including R245fa, R114, R600, and R236fa, and a proton exchange membrane (PEM) electrolyzer for hydrogen generation. A comprehensive thermo-economic analysis is performed on the system performance.…”
Section: Figure 10mentioning
confidence: 99%
“…The fresh water production capacity of proposed system is 0.662 kg/s. [240] • • • For generating power and hydrogen, a modification of organic Rankine cycle (ORC) with a regeneration has been utilized. As indicated in the results, the highest energy and exergy efficiencies belong to R245fa, which are 3.511% and 67.58% respectively.…”
Section: Exergy Analysismentioning
confidence: 99%