Model of the expansion process for R245fa in an Organic Rankine Cycle (ORC)

Abstract An Organic Rankine Cycle (ORC) is considered as one of the most environmental-friendly ways to convert different kinds of low temperature energies, i.e. solar, geothermal, biomass and thermal energy of exhaust gases into electrical energy. Two important facts about the ORC must be considered: An organic fluid is selected as the working fluid and a high expansion ratio is usually presented in the machinery due to thermodynamic and efficiency factors. In the past, the pre-design of turbomachinery has been based on the usage of ideal fluid laws, but the real gas effects have a significant influence in the ORC working condition, due to its proximity to the saturation vapor line. In this article, the Equations of State (EoS) (Ideal gas, Redlich-Kwong-Soave and Peng–Robinson) have been evaluated in a typical ORC expansion in order to observe the inaccuracies of the ideal gas model with different thermodynamic variables. Finally an isothermal process followed by an isochoric process is proposed to reproduce the thermodynamic process of the organic fluid expansion by means of simpler equations. In the last point of this paper, several examples of this expansion process have been calculated, in order to analyze the proposed methodologies. It has been concluded that in typical expansion process of ORC (2.5 MPa-0.1 MPa and 1.6MPa-0.1 MPa), the PR and RKS equations show deviations between 6% and 8% in specific energy. These deviations are very low compared with the ideal gas equation whose deviations are above 100%.

[1]  T. M. Yue,et al.  Design and characteristic analysis of supersonic nozzles for high gas pressure laser cutting , 1997 .

[2]  Roland Span,et al.  Short Fundamental Equations of State for 20 Industrial Fluids , 2006 .

[3]  Stefano Rebay,et al.  Real-Gas Effects in ORC Turbine Flow Simulations: Influence of Thermodynamic Models on Flow Fields and Performance Parameters , 2006 .

[4]  D. A. Kouremenos,et al.  Sound velocity and isentropic exponents for gases with different acentric factors by using the Redlich-Kwong-Soave equation of state , 1987 .

[5]  Ron Hughes,et al.  Computer simulation of BTEX emission in natural gas dehydration using PR and RKS equations of state with different predictive mixing rules , 2004, Environ. Model. Softw..

[6]  Marius Paraschivoiu,et al.  Real gas simulation of hydrogen release from a high-pressure chamber , 2005 .

[7]  D. Peng,et al.  A New Two-Constant Equation of State , 1976 .

[8]  James W. Murdock,et al.  Fundamental Fluid Mechanics for the Practicing Engineer , 1993 .

[9]  O. Redlich,et al.  On the thermodynamics of solutions; an equation of state; fugacities of gaseous solutions. , 1949, Chemical reviews.

[10]  Thomas J. Ahrens,et al.  Equation of State , 1993 .

[11]  G. Soave Rigorous and simplified procedures for determining the pure-component parameters in the Redlich—Kwong—soave equation of state , 1980 .

[12]  Ricardo Novella,et al.  HD Diesel engine equipped with a bottoming Rankine cycle as a waste heat recovery system. Part 2: Evaluation of alternative solutions , 2012 .

[13]  D. Brüggemann,et al.  Exergy based fluid selection for a geothermal Organic Rankine Cycle for combined heat and power generation , 2010 .

[14]  Antonio García,et al.  HD Diesel engine equipped with a bottoming Rankine cycle as a waste heat recovery system. Part 1: Study and analysis of the waste heat energy , 2012 .

[15]  Generalized and exact solutions for oblique shock waves of real gases with application to real air , 1989 .

[16]  M. Wendland,et al.  Screening of pure fluids as alternative refrigerants , 2006 .

[17]  V. Maizza,et al.  WORKING FLUIDS IN NON-STEADY FLOWS FOR WASTE ENERGY RECOVERY SYSTEMS , 1996 .

[18]  Eric W. Lemmon,et al.  Thermophysical Properties of Fluid Systems , 1998 .

[19]  M. Pfitzner,et al.  CFD-Simulation of supercritical LOX/GH2 combustion considering consistent real gas thermodynamics , 2009 .

[20]  Andreas Schuster,et al.  Energetic and economic investigation of Organic Rankine Cycle applications , 2009 .

[21]  G. Soave Equilibrium constants from a modified Redlich-Kwong equation of state , 1972 .

[22]  Ulli Drescher,et al.  Fluid selection for the Organic Rankine Cycle (ORC) in biomass power and heat plants , 2007 .

[23]  D. A. Kouremenos The normal shock waves of real gases and the generalized isentropic exponents , 1986 .