Effects of Superheating on Thermodynamic Performance of Organic Rankine Cycles

Recently ORC(Organic Rankine Cycle) has attracted much attention due to its potential in reducing consumption of fossil fuels and its favorable characteristics to exploit low-grade heat sources. In this work thermodynamic performance of ORC with superheating of vapor is comparatively assessed for various working fluids. Special attention is paid to the effects of system parameters such as the evaporating temperature and the turbine inlet temperature on the characteristics of the system such as maximum possible work extraction from the given source, volumetric flow rate per 1 kW of net work and quality of the working fluid at turbine exit as well as thermal and exergy efficiencies. Results show that for a given source the thermal efficiency increases with decrease of the superheating but exergy efficiency may have a maximum value with respect to the superheating of the working fluid. Results also show that in selection of working fluid it is required to consider various criteria of performance characteristics as well as thermal efficiency.

Authors:



References:
[1] Y.C. Choi, T.J. Park, J.C. Hong, S.Y. Cho, A study on the characteristics
of waste heat from the industrial complexes for residential and commercial
sectors, Energy Eng. J. 8(1999) 242-247(Korean).
[2] N.A. Lai, M. Wendland, J. Fisher, Working fluids for high temperature
organic Rankine cycle, Energy 36(2011) 199-211.
[3] T.C. Hung, T.Y. Shai, S.K. Wang, A review of organic Rankine cycles
(ORCs) for the recovery of low-grade waste heat, Energy 22(1997)
661-667.
[4] U. Drescher, D. Brueggemann, Fluid selection for the organic Rankine
cycle (ORC) in biomass power and heat plants, Applied Thermal Eng.
27(2007) 223-228.
[5] Y. Dai, J. Wang, L. Gao, Parametric optimization and comparative study
of organic Rankine cycle (ORC) for low grade waste heat recovery, Energy
Convs. Mgmt. 50(2009) 576-582.
[6] T.C. Hung, S.K. Wang, C.H. Kuo, B.S. Pei, K.F. Tsai, A study of organic
working fluids on system efficiency of an ORC using low-grade energy
sources, Energy 35(2010) 1403-1411.
[7] F. Heberle, D. Brueggemann, Exergy based fluid selection for a geothermal
organic Rankine cycle for combined heat and power generation,
Applied Thermal Eng. 30(2010) 1326-1332.
[8] Tchanche B.F, Papadakis G, Frangoudakis A : "Fluid selection for a lowtemperature
solar organic Rankine cycle," Applied Thermal Eng., Vol.
29, 2009, pp. 2468-2476.
[9] T. Yang, G.J. Chen, T.M. Guo, Extension of the Wong- Sandler mixing
rule to the three-parameter Patel-Teja equation of state: Application up to
the near-critical region, Chem. Eng. J. 67(1997) 27-36.
[10] J. Gao, L.D. Li, Z.Y. Zhu, S.G. Ru S.G, Vapor-liquid equilibria calculation
for asymmetric systems using Patel-Teja equation of state with a new
mixing rule, Fluid Phase Equilibria 224(2004) 213- 219.
[11] C.L. Yaws, Chemical properties handbook, McGraw- Hill (1999).