2020
DOI: 10.1016/j.renene.2020.01.038
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Exergoeconomic analysis of zeotropic mixture on the new proposed organic Rankine cycle for energy production from geothermal resources

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Cited by 22 publications
(5 citation statements)
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“…To this purpose, the energy content of the organic fluid at the exit of the turbine is exploited (4-4*) to preheat the liquid before the entrance in the evaporator (2-2*). Specifically, centrifugal pumps, radial turbine and shell and tube heat exchangers were selected, according to the literature [19,[88][89][90]. Figure 2b The performances of the geothermal-driven ORC were characterised by adopting a thermodynamic model developed by the authors in the last years [16,29,91].…”
Section: Organic Rankine Cycle (Orc) Unitmentioning
confidence: 99%
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“…To this purpose, the energy content of the organic fluid at the exit of the turbine is exploited (4-4*) to preheat the liquid before the entrance in the evaporator (2-2*). Specifically, centrifugal pumps, radial turbine and shell and tube heat exchangers were selected, according to the literature [19,[88][89][90]. Figure 2b The performances of the geothermal-driven ORC were characterised by adopting a thermodynamic model developed by the authors in the last years [16,29,91].…”
Section: Organic Rankine Cycle (Orc) Unitmentioning
confidence: 99%
“…where p j is the operating pressure. The coefficients b 1,j , b 2,j , c 1,j , c 2,j , c 3,j and the material factors F M,j are shown in Table 2 [19,[88][89][90].…”
Section: Economic Analysismentioning
confidence: 99%
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“…The highest exergy efficiency of 41% was obtained using R600a, which was 9.4% higher when compared with a single-stage cycle. Kazemi and Samadi [112], and Samadi and Kazemi [113] proposed an ORC as shown in Figure 11, using isobutane, R123, and isobutane/isopentane. The maximum energy and exergy efficiencies were obtained using R123, achieving values of 15.31% and 54.25%, respectively.…”
Section: Two-stage Orcmentioning
confidence: 99%
“…Their considered system was an ORC as an upstream cycle, and an absorption chiller as a downstream cycle. Samadi and Kazemi [20] studied a new combined ORC and geothermal cycle with a zeotropic working fluid exergoeconomically. They also optimized the operating parameters of the cycle, and found that increasing the isobutane mole fraction in the isobutane/isopentane mixture causes a reduction in economic return on investment.…”
Section: Introductionmentioning
confidence: 99%