Investigation of the potential of application of single effect and multiple effect absorption cooling systems

Abstract Owing to the serious environmental problems and the price of the traditional energy resources the use of industrial waste heat or the renewable energy, especially the solar energy, as the driving force for vapour absorption cooling systems is continuously increasing. A particular attention was given to single effect cycle. The main objective of higher effect cycle is to increase system performance when high temperature heat source is available. The purpose of the present study was to investigate the potential for the application of single effect double effect and triple effect absorption cooling cycles for production chilled water. For the three systems identical cold output of 300 kW is used. Simulation results were used to study the influence of the various operating parameters on the performance coefficient, exergetic efficiency and the ratio of mass flow rate of refrigerant generated to the heat supplied of the three systems. It is concluded that the COP of double effect system is approximately twice the COP of single effect system and that the COP of triple effect system is slightly less than thrice the COP of single effect system. The exergetic efficiency of double effect system and triple effect system increase slightly compared to the exergetic efficiency of single effect system. It is found that for each condenser and evaporator temperature, there is an optimum generator temperature. At this point the COP and exergetic efficiency of the systems become maximum. Triple effect system generates more vapour refrigerant per unit heat supplied as compared with single effect and double effect systems.

[1]  S. Renganarayanan,et al.  Modelling of steam fired double effect vapour absorption chiller using neural network , 2006 .

[2]  Da-Wen Sun,et al.  Comparison of the performances of NH3-H2O, NH3-LiNO3 and NH3-NaSCN absorption refrigeration systems , 1998 .

[3]  S. A. Sherif,et al.  Thermodynamic analysis of a lithium bromide/water absorption system for cooling and heating applications , 2001 .

[4]  Young Jin Kim,et al.  A study on the advanced performance of an absorption heater/chiller with a solution preheater using waste gas , 2003 .

[5]  B. Agnew,et al.  Exergy analysis: an absorption refrigerator using lithium bromide and water as the working fluids , 2000, Applied Thermal Engineering.

[6]  T. J. Kotas,et al.  The Exergy Method of Thermal Plant Analysis , 2012 .

[7]  Adnan Sözen,et al.  Effect of heat exchangers on performance of absorption refrigeration systems , 2001 .

[8]  Rabah Gomri,et al.  Second law analysis of double effect vapour absorption cooler system , 2008 .

[9]  Xiao Feng,et al.  Thermo-economical analysis between new absorption-ejector hybrid refrigeration system and small double-effect absorption system , 2002 .

[10]  A. Bejan Advanced Engineering Thermodynamics , 1988 .

[11]  Felix Ziegler,et al.  Simulation of the compressor-assisted triple-effect H2O/LiBr absorption cooling cycles , 2002 .

[12]  Donald C. Erickson,et al.  Triple effect absorption cycles [refrigeration heat pumps] , 1996, IECEC 96. Proceedings of the 31st Intersociety Energy Conversion Engineering Conference.

[13]  M. P. Maiya,et al.  Thermodynamic comparison of water-based working fluid combinations for a vapour absorption refrigeration system , 1998 .

[14]  Muhsin Kilic,et al.  Theoretical study on the effect of operating conditions on performance of absorption refrigeration system , 2007 .

[15]  Y. Kaita,et al.  Simulation results of triple-effect absorption cycles , 2002 .

[16]  Rabah Gomri,et al.  Second law comparison of single effect and double effect vapour absorption refrigeration systems , 2009 .

[17]  Ruzhu Wang,et al.  Performance prediction of a solar/gas driving double effect LiBr–H2O absorption system , 2004 .

[18]  P. E. Liley,et al.  Steam and Gas Tables with Computer Equations , 1984 .

[19]  Soteris A. Kalogirou,et al.  Exergy analysis of lithium bromide/water absorption systems , 2005 .

[20]  J. Pátek,et al.  A computationally effective formulation of the thermodynamic properties of LiBr-H2O solutions from 273 to 500 K over full composition range , 2006 .

[21]  Michael J Tierney,et al.  Options for solar-assisted refrigeration—Trough collectors and double-effect chillers , 2007 .

[22]  M. J. Moran,et al.  Thermal design and optimization , 1995 .