Thermodynamic analysis of a solar-based multi-generation system with hydrogen production

Abstract Thermodynamic analysis of a renewable-based multi-generation energy production system which produces a number of outputs, such as power, heating, cooling, hot water, hydrogen and oxygen is conducted. This solar-based multi-generation system consists of four main sub-systems: Rankine cycle, organic Rankine cycle, absorption cooling and heating, and hydrogen production and utilization. Exergy destruction ratios and rates, power or heat transfer rates, energy and exergy efficiencies of the system components are carried out. Some parametric studies are performed in order to examine the effects of varying operating conditions (e.g., reference temperature, direct solar radiation and receiver temperature) on the exergy efficiencies of the sub-systems as well as the whole system. The solar-based multi-generation system which has an exergy efficiency of 57.35%, is obtained to be higher than using these sub-systems separately. The evaluation of the exergy efficiency and exergy destruction for the sub-systems and the overall system show that the parabolic dish collectors have the highest exergy destruction rate among constituent parts of the solar-based multi-generation system, due to high temperature difference between the working fluid and collector receivers.

[1]  G. Naterer,et al.  Upgrading of Waste Heat for Combined Power and Hydrogen Production With Nuclear Reactors , 2010 .

[2]  I. Dincer Refrigeration Systems and Applications , 2003 .

[3]  Ibrahim Dincer,et al.  Recent Canadian advances in nuclear-based hydrogen production and the thermochemical Cu–Cl cycle , 2009 .

[4]  Fahad A. Al-Sulaiman,et al.  Trigeneration: A comprehensive review based on prime movers , 2011 .

[5]  Ibrahim Dincer,et al.  Sustainable Energy Systems and Applications , 2011 .

[6]  I. Dincer Renewable energy and sustainable development: a crucial review , 2000 .

[7]  Ö Ercan Ataer,et al.  Comparative study of irreversibilities in an aqua-ammonia absorption refrigeration system , 1991 .

[8]  Ibrahim Dincer,et al.  Performance analysis of an industrial waste heat‐based trigeneration system , 2009 .

[9]  Ibrahim Dincer,et al.  Exergy: Energy, Environment and Sustainable Development , 2007 .

[10]  Ibrahim Dincer,et al.  Environmental and sustainability aspects of hydrogen and fuel cell systems , 2007 .

[11]  Hasan Hüseyin Erdem,et al.  Thermodynamic model for exergetic performance of a tubular SOFC module , 2009 .

[12]  Feridun Hamdullahpur,et al.  Exergy analysis of an integrated solid oxide fuel cell and organic Rankine cycle for cooling, heating and power production , 2010 .

[13]  Ibrahim Dincer,et al.  Exergy Analysis of an Industrial Waste Heat Recovery Based Cogeneration Cycle for Combined Production of Power and Refrigeration , 2009 .

[14]  Mohand Tazerout,et al.  Thermodynamic analysis of tri-generation with absorption chilling machine , 2003 .

[15]  Isabel Malico,et al.  Design of a trigeneration system using a high‐temperature fuel cell , 2009 .

[16]  Gosse Stephane,et al.  UO 2 と炭素間の高温相互作用:超高温原子炉のTRISO粒子への応用 , 2010 .

[17]  Ibrahim Dincer,et al.  Sustainability aspects of hydrogen and fuel cell systems , 2011 .

[18]  Ibrahim Dincer,et al.  Greenhouse gas emission and exergo-environmental analyses of a trigeneration energy system , 2011 .

[19]  G. Naterer Second Law viability of upgrading waste heat for thermochemical hydrogen production , 2008 .

[20]  Olav Bolland,et al.  Thermodynamic analysis on post-combustion CO2 capture of natural-gas-fired power plant , 2011 .

[21]  Fahad A. Al-Sulaiman,et al.  Exergy modeling of a new solar driven trigeneration system , 2011 .

[22]  I. Dincer,et al.  A simple model for heat and mass transfer in absorption cooling systems (ACSs) , 1996 .