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制冷剂比定压热容的计算分析 被引量:2

Calculation and analysis on isobaric specific heat for refrigerants
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摘要 利用精确度高的P-R状态方程和M-H81状态方程,采用余函数法对制冷剂的比定压热容进行了理论推算和比较分析。文中选用了10种纯制冷剂和4种混合制冷剂进行了详细的计算和比较,计算结果表明:在气相区,2个状态方程模型的计算精度均在3%左右;在液相区,M-H81型方程模型明显优于P-R方程,其计算精度在10%以内。M-H81型方程模型比P-R方程优越,能更好地预测更宽广温度和压力范围的流体比定压热容。文中的工作初步验证了利用状态方程推算实际流体比定压热容的可行性,为其他基础物性的理论预测提供了坚实的理论思路。 Based on P-R equation of state and M-H81 equation of state with high accuracy,detailed calculation and analysis were made by utilizing residual function method.10 pure refrigerants and 4 mixing refrigerants were chosen and compared with experimental results.The calculation results show that in vapor-phase region,the estimation precision is about 3% for both models;while in liquidphase region,M-H81 EOS model is better than P-R EOS model with an estimation precision of less than 10%.M-H81 equation model is more appropriate than P-R equation model to make precise calculation within a broader temperature and pressure range.The study validates the feasibility of theoretical method,and can be a guideline for further study on other basic thermophysical properties.
出处 《化学工程》 EI CAS CSCD 北大核心 2008年第5期48-50,共3页 Chemical Engineering(China)
基金 国家自然科学基金资助项目(50376049 50323001) 教育部新世纪人才支持计划(NCET-04-0925)
关键词 比定压热容 P-R状态方程 M-H81状态方程 推算 制冷剂 isobaric specific heat P-R equation of state M-H81 equation of state estimation refrigerants
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参考文献17

  • 1杨亚晶,何茂刚,张颖.混合制冷剂比定压热容的理论推算[J].化学工程,2007,35(10):42-45. 被引量:5
  • 2Peng D Y, Robinson D B. A new two-constant equation of state[J]. Ind Eng Chem Fundam,1976,15(3): 159--165.
  • 3侯虞钧 张彬 等.马丁-侯状态方程向液相发展[J].化工学报,1981,1:9-9.
  • 4阴建民,何茂刚,刘咸定,刘志刚.共沸与近共沸混合工质CFCs替代物的热力学分析[J].工程热物理学报,1994,15(2):137-140. 被引量:14
  • 5段远源,林鸿,张庆麟,张秋芳.HFC混合物二元交互作用系数研究[J].工程热物理学报,2004,25(2):197-200. 被引量:5
  • 6Turk M, Crone M, Bier K. Mixing behaviour of a mixture of equal amounts of substance of 1,1,1, 2-tetrafluoroethane and 1,1-difluoroethane[ J]. J Chem Thermodynamics, 1996,28 (10) : 1 179--1 194.
  • 7Saitoh A, Nakagawa S, Sato H, et al. Isobaric heat capacity data for liquid HFC-134a[J]. J Chem Eng Data, 1990,35 (2) : 107--110.
  • 8Wirbser H, Brauning G, GUrtner J, et al.Flow-calorlmetrlc specific heat capacities and Joule-Thomson ooefficlents of CF3CHFCH3 (R227)-a new working fluid in energy technics at pressures up to 15 MPa and temperatures between 253 K and 423 K[J]. J Chem Thermodynamics, 1992,24 (7) :761--772.
  • 9Baginskii A V, Stankus S V. Thermodynamic and transport properties of liquid HFC-227ea[J]. Int J Thermophys ,2003,24 (4) :953-961.
  • 10Kubota H, Sotanl T, Kunimoto Y. Isobaric specific heat capacity of difluoromethane at pressure up to 0.5 MPa[ J ]. Fluid Phase Equillb, 1995,104 : 413-419.

二级参考文献15

  • 1阴建民,何茂刚,刘咸定,刘志刚.共沸与近共沸混合工质CFCs替代物的热力学分析[J].工程热物理学报,1994,15(2):137-140. 被引量:14
  • 2项红,工程热物理学报,1993年,14卷,2期,117页
  • 3朴春成,博士学位论文,1991年
  • 4谭连城,工程热物理学报,1985年,16卷,2期,113页
  • 5Peng D Y,Ind Eng Chem Fundam,1976年,15卷,3期,159页
  • 6Viorel Feroiu, Dan Geana. Volumetric and thermodynamic properties for pure refrigerants and refrigerant mixtures from cubic equation of state[ J ]. Fluid Phase Equilibria, 2003,207(1-2) :283-300.
  • 7de Monte F. Calculation of thermodynamic properties of R407C and R410A by the Martin-Hou equation of statepart Ⅰ . Theoretical development[J]. Int J Refrig,2002, 25(3) :306-313.
  • 8de Monte F. Calculation of thermodynamic properties of R407C and R410A by the Martin-Hou equation of statepart Ⅱ: Technical interpretation[J]. Int J Refrig, 2002, 25 (3) :314-329.
  • 9Peng D Y, Robinson D B. A new two-constant equation of state[J]. Ind Eng Chem Fundam, 1976, 15(3): 159-165.
  • 10Turk M, Crone M, Bier K. Mixing behaviour of a mixture of equal amounts of substance of 1,1,1,2-tetrafluoroethane and 1,1-difluoroethane [ J ]. J Chem Thermodynamics, 1996,28(10):1 179-1 194.

共引文献28

同被引文献48

  • 1晋欣桥,周兴禧,徐大中.非共沸混合制冷剂热力参数的计算[J].流体机械,1994,22(3):62-64. 被引量:5
  • 2刘晖,郁永章.立方型状态方程计算R123的热力性质[J].流体机械,1995,23(4):61-62. 被引量:1
  • 3Chapman S, Cowling T G. The Mathematical Theory of Non-Uniform Gases. New York: Cambridge, 1939
  • 4Cohen Y, Sandler S I. The Viscosity and Thermal Conductivity of Simple Dense Gases. Ind. Eng. Chem. Fundam., 1980, 19(2): 186-188
  • 5Hanley H J M, Haynes W M, McCarty R D. The Viscosity and Thermal Conductivity Coefficients for Dense Gaseous and Liquid Methane. J. Phys. Chem. Ref. Data, 1977, 6(2): 597-610
  • 6Sheng W, Chen G J, Lu H C. Predication of Transport Properties of Dense Gases and Liquids by Peng- Robinson(PR) Equation of State. Int. J. of Thermophysics, 1989, 10(1): 133-144
  • 7Sheng W, Lu B C Y. Calculation of Shear Viscosity of Mixtures by Means of an Equation of State, Advances in Cryogenic Engineering, 1990, 35(Pt.B): 1533-1540
  • 8Jossi J A, Stiel L I, Thodos G. The Viscosity of Non-Polar Substances in the Dense Gaseous and Liquid Regions. J. AIChE, 1962, 8(59): 59-62
  • 9Stiel L I, Thodos G. The Viscosity of Polar Substances in the Dense Gaseous And Liquid Regions. J. AIChE, 1964, 10(2): 275-277
  • 10Stiel L I, Thodos G. Thermal Conductivity of Nonpolar Substances in the Dense Gaseous and Liquid Regions. AIChE J., 1964, 10(1): 26-30

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