Vapor-liquid equilibria and volumetric properties for new working fluid ([C6H11N2][HSO4] + LiBr + H2O) and corresponding binary systems at different temperatures and ambient pressure
暂无分享,去创建一个
[1] Hamid Reza Rafiee,et al. The study of thermodynamic properties of the ternary (1-ethyl-3-methylimidazolium hydrogen sulfate + lithium chloride + water) system and corresponding binary systems at different temperatures and ambient pressure , 2016 .
[2] J. Rodríguez,et al. Thermodynamic evaluation of new absorbent mixtures of lithium bromide and organic salts for absorption refrigeration machines , 2006 .
[3] G. Kell. Density, thermal expansivity, and compressibility of liquid water from 0.deg. to 150.deg.. Correlations and tables for atmospheric pressure and saturation reviewed and expressed on 1968 temperature scale , 1975 .
[4] Felix Ziegler,et al. Recent developments and future prospects of sorption heat pump systems , 1999 .
[5] K. R. Seddon,et al. Ionic liquids: a taste of the future. , 2003, Nature materials.
[6] L. Hepler. Thermal expansion and structure in water and aqueous solutions , 1969 .
[7] Donald G. Miller. Activity Coefficient Derivatives of Ternary Systems Based on Scatchard’s Neutral Electrolyte Description , 2007 .
[8] A. K. Mishra,et al. Apparent molar volumes of some amino acids and peptides in aqueous urea solutions , 1983 .
[9] Kenneth S. Pitzer,et al. Activity Coefficients in Electrolyte Solutions , 2017 .
[10] R. Bhat,et al. Thermodynamic studies of transfer of some amino acids and peptides from water to aqueous glucose and sucrose solutions at 298.15 K , 1988 .
[11] D. G. Archer,et al. The Dielectric Constant of Water and Debye‐Hückel Limiting Law Slopes , 1990 .
[12] G. Sadowski,et al. Measuring and modeling aqueous electrolyte/amino-acid solutions with ePC-SAFT , 2014 .
[13] Mohammed Taghi Zafarani-Moattar,et al. The study of vapor–liquid equilibria of 1-ethyl-3-methyl imidazolium chloride and 1-butyl-3-methyl imidazolium chloride in lithium bromide aqueous solutions and their corresponding binary systems at 298.15K. , 2013 .
[14] C. Jolicoeur,et al. Apparent molal volumes of alkali halides in water at 25.deg.. Influence of structural hydration interactions on the concentration dependence , 1969 .
[15] Reinhard Radermacher,et al. Absorption Chillers and Heat Pumps , 1996 .
[16] Dapeng Hu,et al. Performance simulation of the absorption chiller using water and ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate as the working pair , 2011 .
[17] G. Perron,et al. Thermodynamics of the salting effect; free energies, enthalpies, entropies, heat capacities, and volumes of the ternary systems electrolyte–alcohol–water at 25 °C , 1978 .
[18] W. G. McMillan,et al. The Statistical Thermodynamics of Multicomponent Systems , 1945 .
[19] Wolfgang Wagner,et al. International Equations for the Saturation Properties of Ordinary Water Substance , 1987 .
[20] D. Mihov,et al. Investigation of the Aqueous Lithium and Nickel Selenate System , 1998 .
[21] Yoshiaki Takahashi,et al. Abnormal viscosity increment observed for an ionic liquid by dissolving lithium chloride. , 2008, Journal of Physical Chemistry B.
[22] Liangyu Shi,et al. ABSORPTION REFRIGERATION CYCLE UTILIZING A NEW WORKING PAIR OF IONIC LIQUID TYPE , 2010 .
[23] W. F. Stoecker,et al. Refrigeration and air conditioning , 1958 .
[24] D. G. Archer. Thermodynamic Properties of the NaBr+H2O System , 1991 .
[25] G. Iglesias-Silva,et al. Osmotic and Activity Coefficients Using a Modified Pitzer Equation for Strong Electrolytes 1:1 and 1:2 at 298.15 K , 2002 .
[26] L. André,et al. A thermodynamic model of aqueous electrolyte solution behavior and solid-liquid equilibrium in the Li-H-Na-K-Cl-OH-H2O system to very high concentrations (40 molal) and from 0 to 250 °C , 2015, American Journal of Science.
[27] Robin D. Rogers,et al. Ionic Liquids--Solvents of the Future? , 2003, Science.
[28] H. Rafiee,et al. The study of volumetric, acoustic and transport properties of ionic liquid, 1-butyl-3-methyl imidazolium chloride [Bmim][Cl] in aqueous lithium bromide solutions at T = 298.15–318.15 K , 2014 .
[29] Huen Lee,et al. Vapor pressures and vapor-liquid equilibria of the 2,2,2-trifluoroethanol + quinoline system , 2003 .
[30] H. Cabezas,et al. An improved isopiestic method to determine activities in multicomponent mixtures , 1990 .
[31] G. Scatchard. OSMOTIC COEFFICIENTS AND ACTIVITY COEFFICIENTS IN MIXED ELECTROLYTE SOLUTIONS , 1961 .
[32] Li Jing,et al. Vapor Pressure Measurement of the Ternary Systems H2O + LiBr + [Dmim]Cl, H2O + LiBr + [Dmim]BF4, H2O + LiCl + [Dmim]Cl, and H2O + LiCl + [Dmim]BF4 , 2011 .
[33] H. Rafiee,et al. Study of Apparent Molar Volumes for Ionic Liquid, 1-Ethyl-3-methyl Imidazolium Chloride in Aqueous Lithium Nitrate, Lithium Bromide, and Lithium Chloride Solutions at Temperatures (298.15 to 318.15) K , 2015 .
[34] Zongchang Zhao,et al. Thermodynamic properties of a new working pair: 1-Ethyl-3-methylimidazolium ethylsulfate and water , 2010 .
[35] W. Hamer,et al. Osmotic Coefficients and Mean Activity Coefficients of Uni‐univalent Electrolytes in Water at 25°C , 1972 .
[36] O. Redlich,et al. The Molal Volumes of Electrolytes , 1964 .
[37] Andrei G. Fedorov,et al. Thermodynamic analysis of an absorption refrigeration system with ionic-liquid/refrigerant mixture as a working fluid , 2012 .
[38] K. Pitzer,et al. Thermodynamics of electrolytes. II. Activity and osmotic coefficients for strong electrolytes with one or both ions univalent , 1973 .
[39] H. Hasse,et al. Temperature Dependence of the Density of Aqueous Alkali Halide Salt Solutions by Experiment and Molecular Simulation , 2014 .
[40] C. Christov,et al. Study of (m1LiX + m2CaX2)(aq) wheremidenotes molality andXdenotes Cl, or Br at the temperature 298.15 K , 2000 .
[41] C. Machielsen,et al. Thermophysical properties of the trifluoroethanol-pyrrolidone system for absorption heat transformers , 1993 .
[42] J. Gmehling,et al. Experimental determination and correlation of liquid density data of electrolyte mixtures containing water or methanol , 2003 .
[43] C. Christov. Thermodynamic study of (b1LiBr +b2MgBr2)(aq), wherebdenotes molality, at the temperature 348.15K , 1995 .
[44] E. Clarke,et al. Evaluation of the Thermodynamic Functions for Aqueous Sodium Chloride from Equilibrium and Calorimetric Measurements below 154 °C , 1985 .
[45] C. Balarew,et al. Investigation of the aqueous lithium and magnesium halide systems , 1994 .
[46] Walter J. Hamer,et al. Isotonic Solutions. I. The Chemical Potential of Water in Aqueous Solutions of Sodium Chloride, Potassium Chloride, Sulfuric Acid, Sucrose, Urea and Glycerol at 25°1 , 1938 .