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离子液体型新工质对吸收式制冷循环 被引量:8

ABSORPTION REFRIGERATION CYCLE UTILIZING A NEW WORKING PAIR OF IONIC LIQUID TYPE
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摘要 离子液体[mmim]DMP/CH_3OH溶液是具有一定应用潜力的新型吸收式制冷工质对,基于实验和文献数据,提出了针对该工质对的溶液饱和蒸气压、比热容和过量焓的经验方程,并绘制了p-t-x,h-ω图。在此基础上,对新工质对的单效吸收式制冷循环进行了分析,并与传统工质对进行了对比。结果表明:在一定工况范围内,[mmim]DMP/CH_3OH新工质对在循环倍率、COP等持性参数优于NH_3/H_2O体系,堪与LiBr/H_2O体系相媲美。 [mmim]DMP/CHaOH solution used as a new working pair in absorption refrigeration has wide application potential. Empirical equations of saturated vapor pressure, heat capacity, excess enthalpy about this working pair were obtained based on experimental and literature data, p- t- x, h-w charts were drawn. Base on these, new working pair used in the single-effect absorption refrigeration cycle were studied, and compared with traditional working pairs. The results revealed that [mmim]DMP/CH3OH as working pair is better than NHa/H2O system and is on a par with LiBr/H2O system in circulation ratio, COP and other characteristic parameters in the certain operating conditions.
出处 《工程热物理学报》 EI CAS CSCD 北大核心 2010年第10期1627-1630,共4页 Journal of Engineering Thermophysics
基金 国家高科技发展计划(863计划)项目(No.2007AA05Z259) 国家自然科学基金资助项目(No.50706053)
关键词 离子液体 吸收式制冷 工质对 单效循环 ionic liquid absorption refrigeration working pair single-effect cycle
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参考文献11

  • 1ZHOU Y Z, Robertson A J, Hillhouse J H. Phosphonium and Imidazolium Salts and Methods of Their Preparation: US, WO2004016631 [P]. 2004-02-26.
  • 2李春喜,于春影.室温离子液体的制备方法:中国,2004100968413[P].2004-10-09.
  • 3Yokozeki A. Theoretical Performances of Various Refrigerant-Absorbent Pairs in a Vapor-Absorption Refrigeration Cycle by the Use of Equations of State [J]. Applied Energy, 2005, 80(4): 383- 399.
  • 4Yokozeki A, Mark B S. Vapor-Liquid Equilibria of Ammonia+Ionic Liquid Mixtures [J]. Applied Energy, 2007, 84(12): 1258-1273.
  • 5Cai W H, Sen M, Paolucci S. Dynamic Modelling of an Absorption Refrigeration [C]//Proceedings of IMECE2007. Seattle, Washington, USA: ASME, 2007:1-9.
  • 6Kim K S, Shin B K, Lee H, et al. Refractive Index and Heat Capacity of 1-Butyl-3-Methylimidazolium Bromide and 1-Butyl-3-Methylimidazolium Tetrafluoroborate and Vapor Pressure of Binary Systems for 1-Butyl- 3- Met hylimidzolium Bromide+Trifluoroethanol and 1-Butyl-3-Met hylimidazolium Tetrailuoroborate+Trifluoroethanol [J]. Fluid Phase Equilibria, 2004, 218(2): 215-220.
  • 7ZHAO J, JIANG X C, LI C X, et al. Vapor Pressure Measurement for Binary and Ternary Systems Contain- ing a Phosphoric Ionic Liquid [J]. Fluid Phase Equilibria, 2006, 247(1/2): 190 198.
  • 8Smallwood I M. Handbook of Organic Solvent Properties [DB/OL]. [2009-01-04]. http://knovel.com/web/portel/ browse/display_ EXT.-KNOVEL_ DIS-PLAY_ bookid= 567 & VerticalID =0.
  • 9Pereiro A B, Rodrzguez A. Measurement and Correlation of (Liquid + Liquid) Equilibrium of the Azeotrope (Cyclohexane + 2-Butanone) with Different Ionic Liquids at T = 298.15 K[J]. The Journal of Chemical Thermodynamics, 2008, 40(12): 1282-1289.
  • 10Arce A, Martinez J M, Soto A, et al. Isobaric Vapor-Liquid Equilibria of 1,1-DimethylethoxyButane+Methanol or Ethanol+Water at 101.32 kPa[J]. Fluid Phase Equilibria, 2007, 259(12): 57-65.

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