Parametric study of an absorption refrigeration machine using advanced exergy analysis

An advanced exergy analysis of a water–lithium bromide absorption refrigeration machine was conducted. For each component of the machine, the proposed analysis quantified the irreversibility that can be avoided and the irreversibility that is unavoidable. It also identified the irreversibility originating from inefficiencies within the component and the irreversibility that does not originate from the operation of the considered component. It was observed that the desorber and absorber concentrated most of the exergy destruction. Furthermore, the exergy destruction at these components was found to be dominantly endogenous and unavoidable. A parametrical study has been presented discussing the sensitivity of the different performance indicators to the temperature at which the heat source is available, the temperature of the refrigerated environment, and the temperature of the cooling medium used at the condenser and absorber. It was observed that the endogenous avoidable exergy destruction at the desorber, i.e. the portion of the desorber irreversibility that could be avoided by improving the design and operation of the desorber, decreased when the heat source or the temperature at which the cooling effect was generated increased, and it decreased when the heat sink temperature increased. The endogenous avoidable exergy destruction at the absorber displayed the same variations, though it was observed to be less affected by the heat source temperature. Contrary to the aforementioned two components, the exergy destruction at the evaporator and condenser were dominantly endogenous and avoidable, with little sensitivity to the cycle operating parameters.

[1]  Reinhard Radermacher,et al.  Modeling water/lithium bromide absorption chillers in ASPEN Plus , 2011 .

[2]  Kamaruzzaman Sopian,et al.  Evaluation of adding flash tank to solar combined ejector-absorption refrigeration system , 2013 .

[3]  S. Chungpaibulpatana,et al.  A review of absorption refrigeration technologies , 2001 .

[4]  Jaroslav Pátek,et al.  A simple formulation for thermodynamic properties of steam from 273 to 523 K, explicit in temperature and pressure , 2009 .

[5]  G. Tsatsaronis,et al.  A new approach to the exergy analysis of absorption refrigeration machines , 2008 .

[6]  Noam Lior,et al.  Development of a novel combined absorption cycle for power generation and refrigeration , 2007 .

[7]  Reinhard Radermacher,et al.  Application of waste heat powered absorption refrigeration system to the LNG recovery process , 2009 .

[8]  A. T. Bulgan Optimization of the thermodynamic model of aqua-ammonia absorption refrigeration systems , 1995 .

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

[10]  Da-Wen Sun,et al.  Thermodynamic design data and optimum design maps for absorption refrigeration systems , 1997 .

[11]  Tatiana Morosuk,et al.  Conventional thermodynamic and advanced exergetic analysis of a refrigeration machine using a Voorhees’ compression process , 2012 .

[12]  Berhane H. Gebreslassie,et al.  Exergy analysis of multi-effect water–LiBr absorption systems: From half to triple effect , 2010 .

[13]  Ruzhu Wang,et al.  A novel variable effect LiBr-water absorption refrigeration cycle , 2013 .

[14]  S. C. Kaushik,et al.  Energy and exergy analysis of single effect and series flow double effect water–lithium bromide absorption refrigeration systems , 2009 .

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

[16]  Tatiana Morosuk,et al.  Advanced exergetic evaluation of refrigeration machines using different working fluids , 2009 .

[17]  Georgios A. Florides,et al.  Design and construction of a LiBr–water absorption machine , 2003 .

[18]  Pradeep Bansal,et al.  A novel lithium bromide absorption chiller with enhanced absorption pressure , 2012 .

[19]  Pere Margalef,et al.  Integration of a molten carbonate fuel cell with a direct exhaust absorption chiller , 2010 .

[20]  Derya Burcu Özkan,et al.  Exergy analysis of a solar assisted absorption cooling system on an hourly basis in villa applicatio , 2010 .

[21]  P. Kohl,et al.  Performance Simulation of Ionic Liquid and Hydrofluorocarbon Working Fluids for an Absorption Refrigeration System , 2013 .

[22]  Adnan Sözen,et al.  Prospects for utilisation of solar driven ejector-absorption cooling system in Turkey , 2004 .

[23]  Ahmed Bellagi,et al.  Performance improvement of a butane/octane absorption chiller , 2011 .

[24]  Rabah Gomri,et al.  Investigation of the potential of application of single effect and multiple effect absorption cooling systems , 2010 .

[25]  Silvia A. Nebra,et al.  Exergy calculation of lithium bromide–water solution and its application in the exergetic evaluation of absorption refrigeration systems LiBr‐H2O , 2012 .

[26]  Piero Colonna,et al.  Industrial trigeneration using ammonia–water absorption refrigeration systems (AAR) , 2003 .

[27]  Rosenberg J. Romero,et al.  Thermodynamic analysis of monomethylamine–water solutions in a single-stage solar absorption refrigeration cycle at low generator temperatures , 2001 .

[28]  Lin Fu,et al.  A review of working fluids of absorption cycles , 2012 .

[29]  D. Colorado,et al.  Exergy analysis of a compression–absorption cascade system for refrigeration , 2013 .

[30]  Mortaza Yari,et al.  Energy and exergy analyses of GAX and GAX hybrid absorption refrigeration cycles , 2011 .

[31]  Danxing Zheng,et al.  Energy saving mechanism analysis of the absorption–compression hybrid refrigeration cycle , 2013 .

[32]  Jan Szargut,et al.  Exergy Analysis of Thermal, Chemical, and Metallurgical Processes , 1988 .

[33]  M. Farhadi,et al.  Exergy analysis: Parametric study on lithium bromide—water absorption refrigeration systems , 2007 .

[34]  Jason Wonchala,et al.  Solution procedure and performance evaluation for a water–LiBr absorption refrigeration machine , 2014 .

[35]  Nicolas Galanis,et al.  Simulation of an ammonia–water absorption chiller , 2013 .

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

[37]  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 .