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1,1,1,2,3,3,3-七氟丙烷的热力性质 被引量:2

Thermodynamic properties of 1,1,1,2,3,3,3-heptafluoropropane
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摘要 为获得不破坏臭氧层的环保工质的热物性数据 ,对HFC- 2 2 7ea的热力学性质进行了研究 ,精确测量了 2 43~375 K的饱和蒸气压 ,使用膨胀 -定容法测量了 2 78~ 377K,压力 0 .2 6~ 2 .6 MPa的 HFC- 2 2 7ea的气相 p VT性质 ,温度和压力测量的最大不确定度分别为± 10 m K和± 5 0 0 Pa。使用测量结果关联了 HFC- 2 2 7ea的蒸气压方程 ,导出了维里系数、饱和气相密度、饱和蒸发焓 ,并关联了截断维里型的状态方程用于再现 HFC- 2 2 7ea气相区的热力性质。 heptafluoropropane (HFC 227ea) is a recently introduced, commercially available hydrofluorocarbon (HFC), it can be used as an alternative to halon, and blends containing HFC 227ea are potential alternatives to HCFC 22 and R502. Effective use of HFC 227ea requires that the thermodynamic and transport properties are accurately measured, but there is few data available. The gaseous thermodynamic properties of HFC 227ea are presented in this paper. The vapor pressure of HFC 227ea was measured over the temperature range from 243 to 375 K. The pressure volume temperature (pVT) properties of HFC 227ea in the gaseous phase were measured using Burnett/isochoric methods over the temperature range from 283 to 377 K and pressure range from 0.26 to 2.5 MPa. The maximum uncertainties for temperature and pressure in this work were estimated to be within ±10mK and ±500Pa , respectively. The experimental data was used to develop a vapor pressure equation for HFC 227ea. The virial coefficients, the saturated vapor density and the enthalpy of vaporization for HFC 227ea were also determined.
出处 《清华大学学报(自然科学版)》 EI CAS CSCD 北大核心 2000年第10期73-76,共4页 Journal of Tsinghua University(Science and Technology)
基金 国家自然科学基金项目!(5 990 6 0 0 6 )
关键词 七氯丙烷 维里系数 制冷剂 热力学性质 heptafluoropropane vapor pressure pVT properties virial coefficients saturated vapor density enthalpy of vaporization thermodynamic properties
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参考文献5

  • 1Pátek J,Klomfar J,Prazak J,et al.The (P, , T)behaviour of 1, 1, 1, 2, 3, 3, 3-heptafluoropropane(HFC-227ea) measured with a Burnett apparatus[].Journal of Chemical Thermodynamics.1998
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  • 1陈则韶,陈建新,胡芃,王耀武.多元混合工质泡点和露点的推算研究[J].工程热物理学报,2006,27(z1):41-44. 被引量:3
  • 2朱明善.CFC的替代物及我国的对策[J].化工进展,1993,12(5):1-7. 被引量:7
  • 3陈则韶,胡芃,陈建新,江斌.可推算非共沸多元混合物临界区饱和蒸气压的新方程[J].工程热物理学报,2006,27(3):388-390. 被引量:4
  • 4S Bobbo, R Camporese. Vapor-Liquid Equilibria for Difluoromethane (R32) + and Pentafluoroethane (R125) +1,1,1,3,3,3-Hexafluoropropane (R236fa). J. Chem. Eng.Data, 1999, 44(1): 349-352
  • 5C N Kim, Y M Park. Vapor-Liquid Equilibrium of HFC-32/134a and HFC-125/134a Systems. Int. J. Thermophys., 1999, 20(1): 519-530
  • 6Japanese Association of Refrigeration. JAR Handbook Fundament. fifth ed. Tokyo : Japanese Association of Refrigeration, 1993. 170-211
  • 7Tillner-Roth R, Li J, Yokozeki A, et al. Thermodynamic Properties of Pure and Blended Hydrofluorocarbon (HFC) Refrigerants. Tokyo: the Japan Society of Refrigerating and Air Conditioning Engineers, 1998. 135-810
  • 8国家环境保护总局、保护臭氧层领导小组中国保护臭氧层行动[M].1999,(11).
  • 9联合国环境规划署.精细与专用化学品“ODS替代品、替代技术”专刊.1999,(22).
  • 10Horst Kruse. European research conceming CFC and HCFC substitution[J]. Int. J. Refrig. 1994, 17(3) : 149- 155.

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