期刊文献+

适用于整个区域的 HFC-32 状态方程 被引量:4

New equation of state for difluorome thane (HFC 32) over entire region
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摘要 基于现有的PVT和比热容测量数据,作者提供了一个HFC-32跨接状态方程。本方程适用于压力从零至35MPa,密度从零至1450kgm-3,温度从150K至480K。比较了HFC-32的热力学性质,包括:压力-比容-温度(pvT)、比定容热容、声速、第二维里系数、饱和液密度等的测量值与本状态方程计算值。还给出了HFC-32的饱和蒸气压和饱和液密度的计算式。上述计算式具有较高的精度,可满足工程计算需要。 A 35 term crossover equation of state of HFC 32 has been developed, based on the updated available pressure specific volume temperature ( pvT ) measurements and heat capacity measurements. This equation of state is effective at pressures up to 35 MPa, densities up to 1450 kg·m -3 , and temperatures from 150 K to 480 K, respectively. The accuracy of this equation to calculate the thermodynamic properties such as pvT, saturated liquid density, isochoric heat capacity, speed of sound, second virial coefficient are also presented. Based on the reported experimental data of saturation properties, correlations of vapor pressure and saturated liquid density are also presented. The accuracy of the equations can meet the requirements of engineering applications.
出处 《清华大学学报(自然科学版)》 EI CAS CSCD 北大核心 1998年第5期35-39,共5页 Journal of Tsinghua University(Science and Technology)
基金 国家自然科学基金
关键词 HFC-32 制冷剂 状态方程 热力学性质 HFC 32 refrigerant equation of state thermodynamic properties vapor pressure saturated liquid density specific heat capacity speed of sound 
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参考文献6

  • 1Sun Liqun,J Chem Eng Data,1997年,42卷,4期,795页
  • 2Fu Yidong,Fluid Phase Equilib,1995年,111卷,273页
  • 3项红卫,博士学位论文,1995年
  • 4朱明善,Int J Thermophys,1993年,14卷,1221页
  • 5Qian Z Y,JSME Int J,1993年,36卷,4期,665页
  • 6项红卫,硕士学位论文,1993年

同被引文献24

  • 1李平,马沛生,衣守志,赵志刚,丛霖滋.基团对应状态法(CSGC)用于纯物质饱和蒸气压的估算[J].化工学报,1995,46(3):332-337. 被引量:11
  • 2吴志刚,丁国良,芮银波.制冷剂热力性质的快速计算 Ⅱ.典型工质计算公式[J].上海交通大学学报,2006,40(2):301-305. 被引量:5
  • 3项红卫,谭连城,陈钟颀.新的适用于整个热力面的1,1,1,2-四氟乙烷(R134a)跨接状态方程[J].工程热物理学报,1997,18(1):13-16. 被引量:1
  • 4M Mohanraj, S Jayaraj, C Muraleedharan. Environment friendly alternatives to halogenated refrigerants-A review [J]. Greenhouse Gas Control, 2009, 3(1): 108-119.
  • 5B O Bolaji. Experimental study of R152a and HFC-32 to replace R134a in a domestic refrigerator [ J]. Energy, 2010, 35: 3793-3798.
  • 6Chun-cheng Piao, Masahiro Noguchi. Thermodynamic properties of HFC-32 (difluoromethane) [ J ]. International Journal of Refrigeration, 2001, 24(6): 519-530.
  • 7Elaheh K, Goharshadi, Fatemeh Moosavi. Prediction of thermodynamic properties of some hydrofluoroether refriger- ants using a new equation of state [ J ]. Fluid Phase Equi- libria, 2005, 238 ( 1 ) : 112-119.
  • 8Mark O McLinden, Eric W Lemmon, Richard T Jacobsen. Thermodynamic properties for the ahemative refrigerants [ J ]. International Journal of Refrigeration, 1998, 21 (4) : 322-338.
  • 9Kuwabara S, Aoyama H, Sato H, et al. Vapor-liquid coex- istence curve in the critical region and the critical tempera- tures and densities of difluoromethane and pentafluoroeth- ane [ J ]. J Chem Eng Data, 1995,40 ( 1 ) : 112-116.
  • 10胡欢,谷波,龙琼,曾伟平,张春路.亚临界压力区CO2热力性质及传输特性的快速计算模型[J].上海交通大学学报,2008,42(8):1259-1264. 被引量:6

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