A study of organic working fluids on system efficiency of an ORC using low-grade energy sources

Rankine cycles using organic fluids (as categorized into three groups: wet, dry, and isentropic fluids) as working fluids in converting low-grade energy are investigated in this study. The main purpose is to identify suitable working fluids which may yield high system efficiencies in an organic Rankine cycle (ORC) system. Efficiencies of ORC systems are calculated based on an assumption that the inlet condition of the working fluid entering turbine is in saturated vapor phase. Parameters under investigation are turbine inlet temperature, turbine inlet pressure, condenser exit temperature, turbine exit quality, overall irrversibility, and system efficiency. The low-grade energy source can be obtained from a solar pond or/and an ocean thermal energy conversion (OTEC) system. Results indicate that wet fluids with very steep saturated vapor curves in T-s diagram have a better overall performance in energy conversion efficiencies than that of dry fluids. It can also be shown that all the working fluids have a similar behavior of the efficiency-condenser exit temperature relationship. Furthermore, an appropriate combination of solar energy and an ORC system with a higher turbine inlet temperature and a lower condenser temperature (as operated deeply under sea level) would provide an economically feasible and environment-friendly renewable energy conversion system.

[1]  Wilfried van Sark,et al.  A New Hybrid Ocean Thermal Energy Conversion-Offshore Solar Pond (OTEC-OSP) Design: A Cost Optimization Approach , 2008, Renewable Energy.

[2]  Howard T. Odum,et al.  Emergy evaluation of an OTEC electrical power system , 2000 .

[3]  W. Worek,et al.  Optimum design criteria for an Organic Rankine cycle using low-temperature geothermal heat sources , 2007 .

[4]  Jinn-Chuang Yang,et al.  Optimal Design of a Pilot OTEC Power Plant in Taiwan , 1991 .

[5]  Tadayoshi Tanaka,et al.  Performance characteristics of barometric-type open-cycle OTEC system , 1996 .

[6]  George Kosmadakis,et al.  Identification of behaviour and evaluation of performance of small scale, low-temperature Organic Rankine Cycle system coupled with a RO desalination unit , 2009 .

[7]  S. K. Wang,et al.  A Review of Organic Rankine Cycles (ORCs) for the Recovery of Low-grade Waste Heat , 1997 .

[8]  Dylan Tanner,et al.  Ocean thermal energy conversion: Current overview and future outlook , 1995 .

[9]  N. Yamada,et al.  Performance simulation of solar-boosted ocean thermal energy conversion plant , 2009 .

[10]  R. Yeh,et al.  Maximum output of an OTEC power plant , 2005 .

[11]  N. Lai,et al.  Working fluids for high-temperature organic Rankine cycles , 2007 .

[12]  D. E. Lennard,et al.  The viability and best locations for ocean thermal energy conversion systems around the world , 1995 .

[13]  Chi-Chuan Wang,et al.  Effect of working fluids on organic Rankine cycle for waste heat recovery , 2004 .

[14]  Santanu Bandyopadhyay,et al.  Process integration of organic Rankine cycle , 2009 .

[15]  Chih Wu,et al.  Intelligent computer aided optimization on specific power of an OTEC Rankine power plant , 1998 .