2019
DOI: 10.1016/j.apenergy.2019.113408
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Modelling system integration of a micro solar Organic Rankine Cycle plant into a residential building

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Cited by 42 publications
(13 citation statements)
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“…The study is performed by means of a thermodynamic and economic analysis focusing on the energetic, exergetic, and economic performances. Several reasonable assumptions below are defined to simplify the computation process [37][38][39]: (1) each component and operating point is under equilibrium and in a steady-state condition; (2) heat losses and pressure losses are neglected in the pipes and in all components; (3) the isentropic efficiencies of the expander, pump, and generator are assumed to be 0.7, 0.8, and 0.9, respectively; (4) the changes in the kinetic and potential energy of the fluids Energies 2020, 13, 1830 6 of 19 can be neglected; (5) the pinch point temperature differences (T pp ) in the gas heater, preheater, and regenerator are set to be 30 • C, 5 • C, and 15 • C; and (6) temperatures of the condensation process and the ambient are set at 25 • C to guarantee that CO 2 can be condensed stably during the phase change process. The properties of the working fluid are derived from the REFPROP-NIST [40].…”
Section: Mathematical Modelingmentioning
confidence: 99%
“…The study is performed by means of a thermodynamic and economic analysis focusing on the energetic, exergetic, and economic performances. Several reasonable assumptions below are defined to simplify the computation process [37][38][39]: (1) each component and operating point is under equilibrium and in a steady-state condition; (2) heat losses and pressure losses are neglected in the pipes and in all components; (3) the isentropic efficiencies of the expander, pump, and generator are assumed to be 0.7, 0.8, and 0.9, respectively; (4) the changes in the kinetic and potential energy of the fluids Energies 2020, 13, 1830 6 of 19 can be neglected; (5) the pinch point temperature differences (T pp ) in the gas heater, preheater, and regenerator are set to be 30 • C, 5 • C, and 15 • C; and (6) temperatures of the condensation process and the ambient are set at 25 • C to guarantee that CO 2 can be condensed stably during the phase change process. The properties of the working fluid are derived from the REFPROP-NIST [40].…”
Section: Mathematical Modelingmentioning
confidence: 99%
“…Similar work was performed by Ramos et al [28] who maximized the electrical power considering the operational limits of the solar collector of two systems flat-plate solar collector (FPCs-ORC) and evacuated-tube collector-ORC (ETCs-ORC). Arteconi et al [29] studied the influence of the electrical and thermal performance of an ORC system with evacuated tube solar collector and storage tank.…”
Section: Introductionmentioning
confidence: 99%
“…ORC technology is similar to the classic Rankine cycle but uses an organic liquid instead of water. This technology allows efficient use of heat sources with low thermal potential, such as biomass, geothermal energy, and solar energy [22][23][24]. In this case, the heat input to the system can be delivered by several renewable energy sources available locally, e.g., solar energy and biomass [25,26].…”
Section: Introductionmentioning
confidence: 99%