2020
DOI: 10.3390/en13010267
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Advance Exergo-Economic Analysis of a Waste Heat Recovery System Using ORC for a Bottoming Natural Gas Engine

Abstract: This manuscript presents an advanced exergo-economic analysis of a waste heat recovery system based on the organic Rankine cycle from the exhaust gases of an internal combustion engine. Different operating conditions were established in order to find the exergy destroyed values in the components and the desegregation of them, as well as the rate of fuel exergy, product exergy, and loss exergy. The component with the highest exergy destroyed values was heat exchanger 1, which is a shell and tube equipment with … Show more

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Cited by 36 publications
(16 citation statements)
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“…See Equation 7for the specific flow rates of exergy. After calculating fuel and product of the equipment, Ochoa et al [42], further outputs of exergy analysis, i.e., exergy destruction ( . E D ) and exergetic efficiency (ψ k ) of each component can be determined from Equations (8) and (9).…”
Section: Thermodynamic Modelingmentioning
confidence: 99%
“…See Equation 7for the specific flow rates of exergy. After calculating fuel and product of the equipment, Ochoa et al [42], further outputs of exergy analysis, i.e., exergy destruction ( . E D ) and exergetic efficiency (ψ k ) of each component can be determined from Equations (8) and (9).…”
Section: Thermodynamic Modelingmentioning
confidence: 99%
“…The continuous increase in greenhouse effects in the energy field [1,2], the potential danger that represents the future of this trend, and the continuous rise in this kind of energy production boost the development of new trends of energy generation (NTEG), which lead to energy transition [3][4][5]. NTEG will be independent of hydrocarbons and fossil fuels because research on clean energy acquisition methods is on the rise, offering reliable solutions to the current problem [6,7].…”
Section: Introductionmentioning
confidence: 99%
“…The optimization results allowed the maximum output power to be 99.52 kW when the pinch point temperatures of the evaporator and condenser were 35 • C and 16 • C, respectively. In their other work [41], exergo-economic analysis was proved to be a powerful method to identify the irreversibility and highest cost in ORC systems. Besides the mostly studied subcritical ORC systems, trans-critical [42,43] and supercritical ORC systems [44] were also proposed for WHR from marine engine.…”
Section: Introductionmentioning
confidence: 99%