Exergy analysis of a novel air-cooled non-adiabatic absorption refrigeration cycle with NH3–NaSCN and NH3–LiNO3 refrigerant solutions

Abstract This paper presents a methodology of exergy analysis for ammonia-lithium nitrate and ammonia-sodium thiocyanate absorption refrigeration cycle which applies a novel air-cooled type non-adiabatic absorber to improve both the coefficient of performance and exegetic efficiency of the system under air cooling condition. A modified entropy calculation method for NH3/NaSCN and NH3/LiNO3 solutions is presented in this literature and different results are obtained comparing to previous research. In addition to the variation of solution temperature and pressure from specific working state to the reference state, the variation of solution concentration, which was always neglected by previous researchers in ammonia/salt solution exergy calculation, has been taken into account while analyzing the least potential of ammonia/salt solution for doing useful work, and a corresponding approach for specific exergy calculation is presented. The effects of generator temperature, absorber outlet temperature, absorber efficiency and other system parameters on system exergetic efficiency have been discussed in this study. Analysis results indicate that relatively high system performance can be obtained by air-cooled type ammonia/salt absorption refrigeration cycles when non-adiabatic absorbers are applied in these systems.

[1]  Joseph F. Zemaitis,et al.  Handbook of aqueous electrolyte thermodynamics : theory & application , 1986 .

[2]  H. Ibrahim Acar,et al.  Thermodynamic analysis of the absorption refrigeration system with geothermal energy: an experimental study , 2000 .

[3]  R. D. Misra,et al.  Thermoeconomic optimization of a single effect water/LiBr vapour absorption refrigeration system , 2003 .

[4]  K Tyagi Second law analysis of NH3?NaSCN absorption refrigeration cycle , 1986 .

[5]  Marc A. Rosen,et al.  First and second law analysis of ammonia/salt absorption refrigeration systems , 2014 .

[6]  T. K. Gogoi,et al.  Exergy based parametric analysis of a combined reheat regenerative thermal power plant and water–LiBr vapor absorption refrigeration system , 2014 .

[7]  Junjie Gu,et al.  Second law-based thermodynamic analysis of ammonia/sodium thiocyanate absorption system , 2010 .

[8]  Sandeep K. S. Gupta,et al.  Thermodynamic feasibility of harvesting data center waste heat to drive an absorption chiller , 2012 .

[9]  Qiqi Tian,et al.  Thermodynamic analysis of a novel air-cooled non-adiabatic absorption refrigeration cycle driven by low grade energy , 2014 .

[10]  L. Olmstead,et al.  VAPOR PRESSURE OF LITHIUM NITRATE: AMMONIA SYSTEM.1 , 1921 .

[11]  Jan Szargut,et al.  Chemical exergies of the elements , 1989 .

[12]  Alberto Coronas,et al.  Densities, Viscosities, Heat Capacities, and Vapor–Liquid Equilibria of Ammonia + Sodium Thiocyanate Solutions at Several Temperatures , 2011 .

[13]  Alberto Coronas,et al.  Densities, Viscosities, and Heat Capacities of Ammonia + Lithium Nitrate and Ammonia + Lithium Nitrate + Water Solutions between (293.15 and 353.15) K , 2008 .

[14]  R. C. Weast CRC Handbook of Chemistry and Physics , 1973 .

[15]  A. Coronas,et al.  Vapor−Liquid Equilibrium of Ammonia + Lithium Nitrate + Water and Ammonia + Lithium Nitrate Solutions from (293.15 to 353.15) K , 2007 .

[16]  R. S. Agarwal,et al.  Thermodynamic properties of lithium nitrate‐ammonia mixtures , 1986 .

[17]  Pradeep K. Sahoo,et al.  Thermoeconomic evaluation and optimization of an aqua-ammonia vapour-absorption refrigeration system , 2006 .

[18]  Syed A.M. Said,et al.  Exergo-economic analysis of a solar driven hybrid storage absorption refrigeration cycle , 2014 .

[19]  Philippe Haberschill,et al.  A numerical model for the dynamic simulation of a recirculation single-effect absorption chiller , 2012 .

[20]  Xianting Li,et al.  Evaluation of ground source absorption heat pumps combined with borehole free cooling , 2014 .

[21]  Majid Amidpour,et al.  Exergoeconomic analysis of double effect absorption refrigeration systems , 2013 .

[22]  W. A. Beckman,et al.  Theoretical performance of an ammonia-sodium thiocyanate intermittent absorption refrigeration cycle , 1968 .

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

[24]  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 .

[25]  W. E. Ibele,et al.  Availability simulation of a lithium bromide absorption heat pump , 1988 .

[26]  C. A. Infante Ferreira,et al.  Thermodynamic and physical property data equations for ammonia-lithium nitrate and ammonia-sodium thiocyanate solutions , 1984 .

[27]  Mehran Ameri,et al.  Energy, exergy, and economic analysis of single and double effect LiBr–H2O absorption chillers , 2014 .

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

[29]  C. A. Infante Ferreira,et al.  Air-cooled LiBr–water absorption chillers for solar air conditioning in extremely hot weathers , 2009 .

[30]  R. Rivero,et al.  Standard chemical exergy of elements updated , 2006 .

[31]  F. Daniels,et al.  Concentrated Solutions of NaSCN in Liquid Ammonia. Solubility, Density, Vapor Pressure, Viscosity, Thermal Conductance, Heat of Solution and Heat Capacity , 1962 .

[32]  J. Tester,et al.  Activity Coefficients of Strong Electrolytes in Aqueous Solutions , 1972 .

[33]  Refrigerating ASHRAE handbook of fundamentals , 1967 .

[34]  D. Morris,et al.  Standard chemical exergy of some elements and compounds on the planet earth , 1986 .