期刊文献+

水和正丙醇二元体系共沸混合物的低温热容 被引量:2

Low-temperature Heat Capacity of the Azeotropic Mixture Composed of Water and n-propanol
在线阅读 下载PDF
导出
摘要 用全自动低温绝热量热计测定了水和正丙醇组成的共沸混合物(x(H2O)=0.568,x(nC3H7OH)=0.432)在80~320K温区的摩尔热容.建立了共沸混合物与温度T的函数关系.结果表明:水和正丙醇组成的共沸混合物在102.04K发生玻璃态转化,在258.17K发生固液相变,并获得了其相应的相变焓和相变熵.计算了以298.15K为基准的该共沸混合物的热力学函数. The molar heat capacities of the azeotropic mixture composed of water and n-propanol were measured by an adiabatic calorimeter in temperature range from 80 to 320?K.The functions of the heat capacity with respect to thermodynamic temperature were established.The glass transition occurred at 102.04?K.The solid-liquid phase transition took place at 258.17?K.The melting enthalpy and entropy were calculated to be 5.869?kJ/mol and 22.73?J/(K·mol),respectively.The thermodynamic functions of the azeotropic mixture relative to 298.15?K were derived based on the relationships of the thermodynamic functions and the function of the measured heat capacity with respect to temperature.
出处 《河北师范大学学报(自然科学版)》 CAS 北大核心 2005年第2期173-176,192,共5页 Journal of Hebei Normal University:Natural Science
基金 国家自然科学基金资助项目(20373072)
关键词 共沸混合物 二元体系 正丙醇 热力学函数 OH 固-液相变 低温热容 组成 温区 玻璃态 adiabatic calorimetry heat capacity azeotropic mixture water n-propanol
  • 相关文献

参考文献14

  • 1OLSON J D.Thermodynamics of hydrogen-bonding mixtures 4:G(E),H-E,S-E and C-P(E) and possible double azeotropy of water plus N-methylenediamine [J].Fluid Phase Equilibria,2001,185(2):209-218.
  • 2JIANG Y J,HAMMOND E G.Toluenesulfonate-acyl esters of ethylene glycol and other 1,2-diols as industrial antioxidants with cupric ion [J].American Oil Chemists Society,2002,79(6):791-796.
  • 3RESA J M,GONZALEZ C,BETOLAZA M A,et al.Behavior of butyl ether as entrainer for the extractive distillation of the azeotropic mixture propanone+diisopropyl:Isobaric VLE data of the azeotropic components with the entrainer [J].Fluid Phase Equilibria,1999,156(1):89-99.
  • 4RESA J M,GONZALEZ C,LANDALUCE S O,et al.Vapor-liquid equilibria for n-propanol+pentyl acetate,vinyl acetate+pentyl acetate and n-propanol+isopentyl acetate [J].Fluid Phase Equilibria,2001,182(2):177-187.
  • 5RESA J M,GONZALEZ C,RUIZ A.Experiments of extractive distillation at laboratory scale for the rupture of the azeotropic mixture acetone+isopropyl ether [J].Separation and Purification Technology,2000,18(2):103-110.
  • 6DEMIREL Y.Estimation of the entropy of vaporization at the normal boiling point for azeotropic mixtures containing water,alcohol or acetic acid [J].Thermochim Acta,1999,339(1):79-85.
  • 7CARTER K L,HASELDEN G G.Reducing running costs in air conditioning [J].Int J Refrig,1999,22(4):442-451.
  • 8RODRIGUEZ D I,PARDILLO F E,GERBAUD V,et al.Synthesis,experiments and simulation of heterogeneous batch distillation processes [J].Computers and Chemical Engineering,2001,25(5):799-806.
  • 9南照东,谭志诚,孙立贤.水-乙醇二元体系共沸混合物的热力学研究[J].物理化学学报,2004,20(6):626-630. 被引量:4
  • 10PARAMO R,ZOUINE M,CASANOVA C.New batch cells adapted to measure saturated heat capacities of liquids [J].J Chem Eng Data,2002,47(3):441-448.

二级参考文献21

  • 1Demirel, Y. Fluid Phase Equilibria, 1993, 86 (1): 1
  • 2Resa, J. M.; González, C.; Betolaza, M. A.; Ruiz, A. Fluid Phase Equilibria, 1999,156(1): 89
  • 3Resa, J. M.; González, C.; Landaluce, S. O.; Lanz, .J.; Fanega,M. Fluid Phase Equilibria, 2001, 182(2): 177
  • 4Resa, J. M.; González, C.; Ruiz, A. Separation and Purification Technology, 2000, 18 (2): 103
  • 5Demirel, Y. Thermochim. Acta, 1999, 339(1 ): 79
  • 6Carter, K. L. Haselden, G. G. Int. J. Refrig., 1999, 22(5): 442
  • 7Rodriguez, I.; Pardillo, E.; Gerbaud, V.; Joulia, X. Computers and Chemical Engineering, 2001, 25(5): 799
  • 8Larkin, J. A. J. Chem. Thermodynamics, 1975, 7(2): 137
  • 9Hideo, O.; Sachio, M. Thermochim. Acta, 1986, 109(1): 145
  • 10Tan, Z. C.; Sun, Y.; Yin, A. X.; Wang, W. B.; Ye, J. C.; Zhou,L. X. J. Thermal Anal., 1995, 45(1 ): 59

共引文献3

同被引文献14

引证文献2

二级引证文献2

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部