离子液体工质对吸收制冷循环研究进展
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摘要
综述了近年来离子液体吸收制冷工质对的研究进展,重点介绍了离子液体工质对的种类、离子液体工质对热物性的测量及离子液体工质对的理论吸收制冷循环性能。
The research progresses in absorption refrigeration cycle using ionic liquid working pairs in recent years are reviewed,with emphasis on the type of ionic liquid working pairs,the measurement of their thermal and physicochemical properties and their theoretical absorption refrigeration cycle performance are introduced.
The research progresses in absorption refrigeration cycle using ionic liquid working pairs in recent years are reviewed,with emphasis on the type of ionic liquid working pairs,the measurement of their thermal and physicochemical properties and their theoretical absorption refrigeration cycle performance are introduced.
引文
[1]Wang Y,Wang C,Feng X.Optimal match between heat source and absorption refrigeration[J]. Computers&Chemical Engineering,2017,102:268-277.
[2]Li J,Liang C,Huang N.Effect of B-Mo-W complex inhibitor on corrosion of mild steel in 55%Li Br solution[J]. Journal of Materials Engineering and Performance,2015,24(11):4456-4461.
[3]Jawahar C P,Saravanan R.Experimental studies on air-cooled NH3-H2O based modified gax absorption cooling system[J].International Journal of Refrigeration,2011,34(3):658-666.
[4]蒋伟燕,余文轴.离子液体的分类,合成及应用[J].金属材料与冶金工程,2008,36(4):51-54.
[5]Wu W D,Wu J,Hou Y,et al.Predicting CO2solubility in imidazole ionic liquids for use in absorption refrigeration systems by using the group contribution equation of state method[J]. International Journal of Thermophysics,2017,38(9):1-14.
[6]Kortenbruck K,Pohrer B,Schluecker E,et al.Determination of the diffusion coefficient of CO2in the ionic liquid[EMIm][NTf2]using online FT-IR measurements[J]. The Journal of Chemical Thermodynamics,2012,47:76-80.
[7]Liu X,Lv N,Bai L,et al.Solubilities of propane and cyclopropane in 1-hexyl-3-methylimidazolium tris(pentafluoroethyl)trifluorophosphate[J].International Journal of Refrigeration,2016,67:69-76.
[8]魏颖,张庆国.离子液体[BMIm][BF4]水溶液粘度性质的研究[J].渤海大学学报:自然科学版,2008,29(2):123-127.
[9]Luo C,Li Y,Chen K,et al. Thermodynamic properties and corrosivity of a new absorption heat pump working pair:Lithium nitrate+1-butyl-3-methylimidazolium bromide+water[J]. Fluid Phase Equilibria,2017,451:25-39.
[10]孙立,郭开华,皇甫立霞.[EMIm]AC和[HMIm]Cl及其水溶液热力学特性实验研究[J].低温物理学报,2011,33(6):467-473.
[11]粟航,郭开华,皇甫立霞,等.强吸水性离子液体-水工质对吸收式制冷循环性能分析[J].制冷学报,2013,34(3):24-30.
[12]Zhang X,Hu Dapeng,Zhao Zongchang.Measurement and prediction of vapor pressure for H2O+CH3OH/C2H5OH+[BMIM][DBP]ternary working fluids[J]. Chinese Journal of Chemical Engineering,2013,21(8):886-893.
[13]Zhang X,Hu D.Performance simulation of the absorption chiller using water and ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate as the working pair[J].Applied Thermal Engineering,2011,31(16):3316-3321.
[14]Dong L,Zheng D,Nie N,et al.Performance prediction of absorption refrigeration cycle based on the measurements of vapor pressure and heat capacity of H2O+[DMIm]DMP system[J]. Applied Energy,2012,98:326-332.
[15]王瑛,李静,王克良,等.含离子液体工质对的吸收式制冷循环特性分析[J].中北大学学报:自然科学版,2016,37(5):511-515.
[16]陈伟,李兰兰,梁世强,等.[MMIm]DMP/CH3OH吸收式制冷热力性能研究[J].工程热物理学报,2013,34(4):689-693.
[17]Wang X,Zhang Y,Wang D,et al.Phase equilibria of trans-1,3,3,3-tetrafluoropropene with three imidazolium ionic liquids[J].Journal of Chemical&Engineering Data,2017,62(6):1825-1831.
[18]Kim S,Kohl P A. Analysis of[HMIm][PF6] and[HMIm][Tf2N] ionic liquids as absorbents for an absorption refrigeration system[J]. International Journal of Refrigeration,2014,48:105-113.
[19]Chen W,Bai Y.Thermal performance of an absorption-refrigeration system with[EMIm]Cu2Cl5/NH3as working fluid[J]. Energy,2016,112(c):332-341.
[20]Wang M,Ferreira C A I.Absorption heat pump cycles with NH3-ionic liquid working pairs[J].Applied Energy,2017,204:819-830.
[21]Ayou D S,Currs M R,Salavera D,et al.Performance analysis of absorption heat transformer cycles using ionic liquids based on imidazolium cation as absorbents with 2,2,2-trifluoroethanol as refrigerant[J].Energy Conversion and Management,2014,84:512-523.
[22]孙立,郭开华,皇甫立霞.离子液体[BMIm][BF4]水溶液比热容及热工特性分析[J].低温物理学报,2011,33(5):381-385.
[23]Chen W,Zhang B,Liu Z,et al.Investigation of the mutual diffusion coefficients of[MMIm]DMP/H2O and[MMIm] DMP/CH3OH at atmospheric pressure[J]. International Journal of Heat and Mass Transfer,2017,111:559-569.
[24]Liu X,Pan P,He M.Vapor-liquid equilibrium and diffusion coefficients of R32+[HMIm][FEP],R152a+[HMIm][FEP] and R161+[HMIm][FEP][J]. Journal of Molecular Liquids,2018,253:28-35.
[25]何丽娟,梁晶晶,张少华.CO2-[EMIm][Tf2N]二元混合体系超额混合焓的预测[J].西安交通大学学报,2015,49(9):99-104.
[26]何丽娟,袁致林,庞贇佶,等.新型低品位热驱动CO2-[EMIm][Tf2N]吸收制冷循环性能[J].河南科技大学学报:自然科学版,2015,36(5):25-29.
[27]何丽娟,黄艳伟,李虹琰.双温低品位热驱动跨临界CO2-[EMIm][Tf2N]吸收制冷系统的性能[J].过程工程学报,2017,17(3):626-631.
[28]Martín,Bermejo M D.Thermodynamic analysis of absorption refrigeration cycles using ionic liquid+supercritical CO2pairs[J].The Journal of Supercritical Fluids,2010,55(2):852-859.
[29]Swarnkar S K,Murthy S S,Gardas R L,et al. Performance of a vapour absorption refrigeration system operating with ionic liquidammonia combination with water as cosolvent[J].Applied Thermal Engineering,2014,72(2):250-257.
[30]王建召,郑丹星.以TFE-[BMIm][Br]为工质对的吸收式制冷循环性能分析[J].工程热物理学报,2008,29(11):1813-1816.
[2]Li J,Liang C,Huang N.Effect of B-Mo-W complex inhibitor on corrosion of mild steel in 55%Li Br solution[J]. Journal of Materials Engineering and Performance,2015,24(11):4456-4461.
[3]Jawahar C P,Saravanan R.Experimental studies on air-cooled NH3-H2O based modified gax absorption cooling system[J].International Journal of Refrigeration,2011,34(3):658-666.
[4]蒋伟燕,余文轴.离子液体的分类,合成及应用[J].金属材料与冶金工程,2008,36(4):51-54.
[5]Wu W D,Wu J,Hou Y,et al.Predicting CO2solubility in imidazole ionic liquids for use in absorption refrigeration systems by using the group contribution equation of state method[J]. International Journal of Thermophysics,2017,38(9):1-14.
[6]Kortenbruck K,Pohrer B,Schluecker E,et al.Determination of the diffusion coefficient of CO2in the ionic liquid[EMIm][NTf2]using online FT-IR measurements[J]. The Journal of Chemical Thermodynamics,2012,47:76-80.
[7]Liu X,Lv N,Bai L,et al.Solubilities of propane and cyclopropane in 1-hexyl-3-methylimidazolium tris(pentafluoroethyl)trifluorophosphate[J].International Journal of Refrigeration,2016,67:69-76.
[8]魏颖,张庆国.离子液体[BMIm][BF4]水溶液粘度性质的研究[J].渤海大学学报:自然科学版,2008,29(2):123-127.
[9]Luo C,Li Y,Chen K,et al. Thermodynamic properties and corrosivity of a new absorption heat pump working pair:Lithium nitrate+1-butyl-3-methylimidazolium bromide+water[J]. Fluid Phase Equilibria,2017,451:25-39.
[10]孙立,郭开华,皇甫立霞.[EMIm]AC和[HMIm]Cl及其水溶液热力学特性实验研究[J].低温物理学报,2011,33(6):467-473.
[11]粟航,郭开华,皇甫立霞,等.强吸水性离子液体-水工质对吸收式制冷循环性能分析[J].制冷学报,2013,34(3):24-30.
[12]Zhang X,Hu Dapeng,Zhao Zongchang.Measurement and prediction of vapor pressure for H2O+CH3OH/C2H5OH+[BMIM][DBP]ternary working fluids[J]. Chinese Journal of Chemical Engineering,2013,21(8):886-893.
[13]Zhang X,Hu D.Performance simulation of the absorption chiller using water and ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate as the working pair[J].Applied Thermal Engineering,2011,31(16):3316-3321.
[14]Dong L,Zheng D,Nie N,et al.Performance prediction of absorption refrigeration cycle based on the measurements of vapor pressure and heat capacity of H2O+[DMIm]DMP system[J]. Applied Energy,2012,98:326-332.
[15]王瑛,李静,王克良,等.含离子液体工质对的吸收式制冷循环特性分析[J].中北大学学报:自然科学版,2016,37(5):511-515.
[16]陈伟,李兰兰,梁世强,等.[MMIm]DMP/CH3OH吸收式制冷热力性能研究[J].工程热物理学报,2013,34(4):689-693.
[17]Wang X,Zhang Y,Wang D,et al.Phase equilibria of trans-1,3,3,3-tetrafluoropropene with three imidazolium ionic liquids[J].Journal of Chemical&Engineering Data,2017,62(6):1825-1831.
[18]Kim S,Kohl P A. Analysis of[HMIm][PF6] and[HMIm][Tf2N] ionic liquids as absorbents for an absorption refrigeration system[J]. International Journal of Refrigeration,2014,48:105-113.
[19]Chen W,Bai Y.Thermal performance of an absorption-refrigeration system with[EMIm]Cu2Cl5/NH3as working fluid[J]. Energy,2016,112(c):332-341.
[20]Wang M,Ferreira C A I.Absorption heat pump cycles with NH3-ionic liquid working pairs[J].Applied Energy,2017,204:819-830.
[21]Ayou D S,Currs M R,Salavera D,et al.Performance analysis of absorption heat transformer cycles using ionic liquids based on imidazolium cation as absorbents with 2,2,2-trifluoroethanol as refrigerant[J].Energy Conversion and Management,2014,84:512-523.
[22]孙立,郭开华,皇甫立霞.离子液体[BMIm][BF4]水溶液比热容及热工特性分析[J].低温物理学报,2011,33(5):381-385.
[23]Chen W,Zhang B,Liu Z,et al.Investigation of the mutual diffusion coefficients of[MMIm]DMP/H2O and[MMIm] DMP/CH3OH at atmospheric pressure[J]. International Journal of Heat and Mass Transfer,2017,111:559-569.
[24]Liu X,Pan P,He M.Vapor-liquid equilibrium and diffusion coefficients of R32+[HMIm][FEP],R152a+[HMIm][FEP] and R161+[HMIm][FEP][J]. Journal of Molecular Liquids,2018,253:28-35.
[25]何丽娟,梁晶晶,张少华.CO2-[EMIm][Tf2N]二元混合体系超额混合焓的预测[J].西安交通大学学报,2015,49(9):99-104.
[26]何丽娟,袁致林,庞贇佶,等.新型低品位热驱动CO2-[EMIm][Tf2N]吸收制冷循环性能[J].河南科技大学学报:自然科学版,2015,36(5):25-29.
[27]何丽娟,黄艳伟,李虹琰.双温低品位热驱动跨临界CO2-[EMIm][Tf2N]吸收制冷系统的性能[J].过程工程学报,2017,17(3):626-631.
[28]Martín,Bermejo M D.Thermodynamic analysis of absorption refrigeration cycles using ionic liquid+supercritical CO2pairs[J].The Journal of Supercritical Fluids,2010,55(2):852-859.
[29]Swarnkar S K,Murthy S S,Gardas R L,et al. Performance of a vapour absorption refrigeration system operating with ionic liquidammonia combination with water as cosolvent[J].Applied Thermal Engineering,2014,72(2):250-257.
[30]王建召,郑丹星.以TFE-[BMIm][Br]为工质对的吸收式制冷循环性能分析[J].工程热物理学报,2008,29(11):1813-1816.