Alternative absorption heat transformer configurations integrated with water desalination system

Abstract Alternative configurations of absorption heat transformer (AHT) systems using LiBr/H2O as the working fluid and integrated with a water purification system are analyzed and optimized thermodynamically. The waste heat from a textile factory is utilized to run the AHT systems and the generated high temperature heat is employed for the purpose of desalination. A computer program is developed in EES (Engineering Equation Solver) to investigate the effects of different parameters on four different configurations of AHT and the desalination system. It is shown that applying different modifications can increase the coefficient of performance (COP) of the AHT and consequently the productivity of the desalination system. The maximum rate of distilled pure water reaches 0.2435 kg/s when waste heat from the condenser is utilized by the evaporator. Finally, the risk of crystallization of LiBr is lowered in the modified configurations.

[1]  Roberto Best,et al.  Single stage and double absorption heat transformers used to recover energy in a distillation column of butane and pentane , 2003 .

[2]  Ugur Atikol,et al.  Overview of Ionic Liquids Used as Working Fluids in Absorption Cycles , 2013 .

[3]  Rajagopal Saravanan,et al.  Exergetic performance of eco friendly absorption heat transformer for seawater desalination , 2011 .

[4]  Rabah Gomri,et al.  Energy and exergy analyses of seawater desalination system integrated in a solar heat transformer. , 2009 .

[5]  Essam E. Khalil Potable water technology development in Egypt , 2001 .

[6]  Lin Shi,et al.  Performance analysis of an absorption heat transformer with different working fluid combinations , 2000 .

[7]  I. Horuz,et al.  Absorption heat transformers and an industrial application , 2010 .

[8]  J. Siqueiros,et al.  Optimum operating conditions for a water purification process integrated to a heat transformer with energy recycling using neural network inverse. , 2009 .

[9]  Mortaza Yari,et al.  Proposal and analysis of a new combined cogeneration system based on the GT-MHR cycle , 2012 .

[10]  Rosenberg J. Romero,et al.  Single-stage and advanced absorption heat transformers operating with lithium bromide mixtures used to increase solar pond's temperature , 2001 .

[11]  I. Horuz,et al.  Single stage and double absorption heat transformers in an industrial application , 2009 .

[12]  Rosenberg J. Romero,et al.  Exergy analysis of an experimental single-stage heat transformer operating with single water/lithium bromide and using additives (1-octanol and 2-ethyl-1-hexanol) , 2011 .

[13]  Zongchang Zhao,et al.  Thermodynamic performance of a double-effect absorption heat-transformer using TFE/E181 as the working fluid , 2005 .

[14]  R. Best,et al.  Thermodynamic design data for absorption heat transformers—Part II. Operating on water-calcium chloride , 1986 .

[15]  Rosenberg J. Romero,et al.  Theoretical and experimental comparison of the performance of a single-stage heat transformer operating with water/lithium bromide and water/Carrol™ , 2002 .

[16]  Wilfrido Rivera,et al.  Exergy analysis of a heat transformer for water purification increasing heat source temperature , 2010 .

[17]  Rajagopal Saravanan,et al.  Experimental studies on absorption heat transformer coupled distillation system , 2011 .

[18]  Erasmo Cadenas,et al.  Exergy analysis of an experimental heat transformer for water purification , 2011 .

[19]  V. Gómez,et al.  Performance modelling of single and double absorption heat transformers , 2010 .

[20]  Dapeng Hu,et al.  Performance analysis of the single-stage absorption heat transformer using a new working pair composed of ionic liquid and water , 2012 .

[21]  Rosenberg J. Romero,et al.  Optimal water purification using low grade waste heat in an absorption heat transformer , 2008 .

[22]  Marc A. Rosen,et al.  Analysis of crystallization risk in double effect absorption refrigeration systems , 2011 .

[23]  Rosenberg J. Romero,et al.  Increase of COP for heat transformer in water purification systems. Part I – Increasing heat source temperature , 2007 .

[24]  Adnan Sözen,et al.  Performance improvement of absorption heat transformer , 2007 .

[25]  Kamel Ghali,et al.  Experimental and theoretical study of an integrated thermoelectric–photovoltaic system for air dehumidification and fresh water production , 2012 .

[26]  Rabah Gomri,et al.  Thermal seawater desalination: Possibilities of using single effect and double effect absorption heat transformer systems , 2010 .

[27]  Mortaza Yari,et al.  A novel cogeneration cycle based on a recompression supercritical carbon dioxide cycle for waste heat recovery in nuclear power plants , 2012 .

[28]  Fengrui Sun,et al.  Optimization between heating load and entropy-production rate for endoreversible absorption heat-transformers , 2005 .

[29]  D. Juárez-Romero,et al.  COP prediction for the integration of a water purification process in a heat transformer: with and without energy recycling , 2008 .

[30]  Wilfrido Rivera,et al.  Experimental study of the use of additives in the performance of a single‐stage heat transformer operating with water–lithium bromide , 2005 .

[31]  Lourdes García-Rodríguez,et al.  Preliminary design and cost analysis of a solar distillation system , 1999 .

[32]  Alberto Coronas,et al.  Purification of seawater using absorption heat transformers with water-(LiBr+LiI+LiNO3+LiCl) and low temperature heat sources , 2004 .