期刊文献+

1,2-丙二醇+丁醇/戊醇/己醇二元系的过量体积和黏度 被引量:1

Excess Molar Volumes and Viscosities of Binary Mixtures Composed of 1,2-Propanediol with Butanol, Pentanol or Hexanol
下载PDF
导出
摘要 常压下测定了1,2-丙二醇分别与丁醇、戊醇和己醇组成的二元系在293.15~318.15 K下的密度和黏度,建立了混合液密度和黏度随温度和组成变化的方程。计算了过量摩尔体积VE,黏度偏差Δη和过量流动活化自由能ΔG*E。结果表明,三个二元系的过量摩尔体积在全浓度范围内均为正值,随温度升高,偏差增大,但发生最大偏差时的溶液组成不同;过量摩尔体积值按丁醇-戊醇-己醇顺序逐渐增大;黏度偏差和过量流动活化自由能三个体系显示了相同的变化关系,均为负值,且都随温度降低而偏差增大。利用Redlich-Kister方程对过量性质进行了关联。分析和讨论了分子间相互作用。 The densities and viscosities of binary mixtures consisting of butanol, pentanol or hexanol with 1,2-propanediol(12PD) were measured using pycnometer and Ubbelohde viscometer at 293.15~318.15 K under atmospheric pressure. The density and viscosity data of the binary mixtures were fitted as functions of composition and temperature. Excess molar volumes(VE), viscosity deviations(Δη) and excess Gibbs energy of activation of viscous flow(ΔG*E) were calculated from the experimental data. The results show that the excess molar volumes are positive over the whole mole fraction range in the temperature range studied for all of the binary mixtures, and the deviation increases as temperature increases. However, the largest deviation varies in different solution compositions. The excess molar volume value increases following an order of butanol-pentanol – hexanol. Both Δη and ΔG*E are negative over the whole mole fraction range in the temperature range studied for all of the binary mixtures, and the deviation increases as temperature decreases. All of the excess properties are correlated by the Redlich-Kister equation and the molecular interactions are analyzed.
出处 《高校化学工程学报》 EI CAS CSCD 北大核心 2016年第2期268-275,共8页 Journal of Chemical Engineering of Chinese Universities
关键词 密度 黏度 过量体积 黏度偏差 过量流动活化自由能 density viscosity excess molar volume viscosity deviation excess Gibbs energy of activation of viscous flow
  • 相关文献

参考文献24

  • 1Kumar D S, Srikanth K, Rao D K. Molecular interactions in the mixture of 2-chloroaniline with equimolar mixture of methanol and isopropanol/isobutanol [J]. Journal of Molecular Liquids, 2007, 136: 90-93.
  • 2Yadav A, Trivedi S, Rai R, et al. Densities and dynamic viscosities of (choline chloride + glycerol) deep eutectic solvent and its aqueous mixtures in the temperature range (283.15-363.15) K [J]. Fluid Phase Equilibria, 2014, 367: 135-142.
  • 3Zhou Y H, Li S N, Zhai Q G, et al. Compositions, densities, and refractive indices for the ternary systems ethylene glycol + NaC1 +H20, ethylene glycol +KC1 +H20, ethylene glycol +RbCI +H20, and ethylene +CsC1 +H20 at 298.15K [J]. J Chem Eng Data, 2010, 55(3): 1289-1294.
  • 4凌锦龙,曹枫,徐敏虹,俞丽丽.乙酸乙酯-1,2-丙二醇二元系的密度、折射率和黏度[J].化工学报,2011,62(5):1191-1196. 被引量:2
  • 5Moosavi M, Motahari A, Omrani A, et al. Thermodynamic study on some alkanediol solutions: measurement and modeling [J]. Thermochimica Acta, 2013, 561:1 - 13.
  • 6Dubey G P, Kaur E Molecular interactions in binary mixtures of 1-butoxy-2-propanol with alcohols at different temperatures: A thermophysical and spectroscopic approach [J]. J Chem Thermodynamics, 2014, 79: 100-108.
  • 7Almasi M, Khosravi L. Excess molar volumes of 1,3-propanediol + (CI-Cs) alkan-l-ols:application of a cubic equation of state [J]. J Serb Chem Soc, 2012, 77(3): 363-370.
  • 8杨得岭,林晓,曹宏斌,李以圭,张懿.3-庚酮+乙酸乙酯、3-庚酮+乙酸丁酯、3-庚酮+TBP、MIBK+TBP二元体系的过量摩尔体积和黏度[J].化工学报,2012,63(8):2327-2340. 被引量:2
  • 9郑博予,房升,何潮洪.丁酮肟-丁酮、正己烷、环己烷二元体系密度和黏度的测定及关联[J].高校化学工程学报,2010,24(6):911-916. 被引量:5
  • 10Zhang H Y, Li S N, Zhai Q G, et al. Solubilities, densities, and refractive indices for the ternary system 1,2-propylene glycol + MNO3 + 1-120 (M=Na, K, Rb, Cs) at 25~C and 35~C [J]. Chem Eng Comm, 2014, 201: 323-337.

二级参考文献71

  • 1张克武,张宇英.液体输运现象新理论Ⅰ液体粘度理论方程和2个定理[J].黑龙江大学自然科学学报,2004,21(3):96-103. 被引量:4
  • 2李楠楠,马沛生,金会义,杨长生.碳酸二甲酯相关二元体系粘度和密度的测定及关联[J].高校化学工程学报,2004,18(6):766-772. 被引量:4
  • 3李猛,刘俊东,那宏壮.丁酮肟的应用及合成进展[J].化学工程师,2006,20(7):42-43. 被引量:15
  • 4Awwad A M,Abu-Daabes M A.Densities,viscosities,and excessproperties of (N-methylmorpholine + cyclohexane,+ benzene,and+ toluene) at T (298.15,303.15,313.15,323.15) K[J].J Chem Thermodyn,2008,40(4):645-652.
  • 5Oswal S L,Gardas R L,Phalak R P.Densities,speeds of sound,isentropic compressibilities,refractive indices and viscosities of binary mixtures of tetrahydrofuran with hydrocarbons at 303.15 K[J].J Mol Liq,2005,116(2):109-118.
  • 6Wei I C,Rowley R L.A local composition model for multicomponent liquid mixture shear viscosity[J].Chem Eng Sci,1985,40(3):401-408.
  • 7Grunberg L,Nissan A.H.Mixture law for viscosity[J].Nature,1949,164(4175):799-800.
  • 8Isdale J D.Symposium on Transport Properties of Fluids and Fluid Mixtures[M].East Kilbride,Glasgow,Scotland:Natl Eng.Lab,1979.
  • 9Gaston-Bonhomme Y,Petrino P,Chevalier J L.UNIFAC-VISCO group contribution method for predicting kinematic viscosity:extension and temperature dependence[J].Chem Eng Sci,1994,49(11):1799-1806.
  • 10Rosana J M,Márcio J E,Cardoso de M,et al.Calculation of viscosity of ternary and quaternary liquid mixtures[J].Ind Eng Chem Res,2001,40(4):1271-1275.

共引文献12

同被引文献2

引证文献1

二级引证文献1

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