Power generation using Organic Rankine Cycle was studied in this paper in case of both low and high temperature cycles, exploiting respectively a geothermal heat source available at 167 °C, and heat available at 300 °C from the combustion of biomass. In particular we assess the feasibility of employing mixture of working fluids, in the case of replacing the typical once-through (OT) evaporator with the pool boiler (PB) technology, typically adopted for pure fluids. The analysis evidenced that in general the OT evaporator shows a slightly improved cycle performance in comparison to the PB and it results in some cases advantageous with respect to the pure working fluid. For instance in case of low temperature cycle, the best thermodynamic performances are obtained with mixture of i-C5 and 75% n-C4 in case of OT evaporator, yielding a recovery efficiency higher than the case with pure i-C5 (7.7 vs. 7.4%) given the relatively higher values of both the recovery factor and cycle efficiency. Implementation of PB did not affect the plant performance significantly which shows the feasibility of having PB with potentially easier control.

Mixture of working fluids in ORC plants with pool boiler evaporator

IORA, Paolo Giulio;INVERNIZZI, Costante Mario
2016-01-01

Abstract

Power generation using Organic Rankine Cycle was studied in this paper in case of both low and high temperature cycles, exploiting respectively a geothermal heat source available at 167 °C, and heat available at 300 °C from the combustion of biomass. In particular we assess the feasibility of employing mixture of working fluids, in the case of replacing the typical once-through (OT) evaporator with the pool boiler (PB) technology, typically adopted for pure fluids. The analysis evidenced that in general the OT evaporator shows a slightly improved cycle performance in comparison to the PB and it results in some cases advantageous with respect to the pure working fluid. For instance in case of low temperature cycle, the best thermodynamic performances are obtained with mixture of i-C5 and 75% n-C4 in case of OT evaporator, yielding a recovery efficiency higher than the case with pure i-C5 (7.7 vs. 7.4%) given the relatively higher values of both the recovery factor and cycle efficiency. Implementation of PB did not affect the plant performance significantly which shows the feasibility of having PB with potentially easier control.
2016
2015
Ateneo di appartenenza
PE2_14 Thermodynamics
PE8_6 Energy systems (production, distribution, application)
Esperti anonimi
Inglese
Internazionale
STAMPA
98
1
9
9
Heat exchanger; Mixture as working fluid; Organic Rankine cycles; Working fluid; Energy Engineering and Power Technology; Industrial and Manufacturing Engineering
http://www.journals.elsevier.com/applied-thermal-engineering/
3
info:eu-repo/semantics/article
262
Rajabloo, Talieh; Iora, Paolo Giulio; Invernizzi, Costante Mario
1 Contributo su Rivista::1.1 Articolo in rivista
none
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11379/484259
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