Reference

Liquid-vapor equilibrium

Liquid-vapor equilibrium. 3-Pentanol - heptane system. Campbell, S. W. (Department of Chemical Engineering, University of South Florida, Tampa, FL 33620-5350, USA). International DATA Series, Selected Data on Mixtures, Series A: Thermodynamic Properties of Non-Reacting Binary Systems of Organic Substances, 32(1), 7 (English) 2004 National Institute of Standards and Technology. CODEN: ISDMAT. ISSN: 0147-1503. DOCUMENT TYPE: Journal CA Section: 68 (Phase Equilibriums, Chemical Equilibriums, and Solutions) The vapor pressures in the binary system were measured at T = 313.15 K. The pressure values are listed together with the mole fraction of 3-pentanol in the liq. phase. The measurements were carried out using a static app. of the Gibbs - Van Ness type. It consists of a Pyrex equil. cell connected to a Ruska pump and suspended in a water bath, in which the temp. was controlled within ±0.02 K.

Liquid-vapor equilibrium

Liquid-vapor equilibrium. 3-Pentanol - benzene system. Campbell, S. W. (Department of Chemical Engineering, University of South Florida, Tampa, FL 33620-5350, USA). International DATA Series, Selected Data on Mixtures, Series A: Thermodynamic Properties of Non-Reacting Binary Systems of Organic Substances, 32(1), 23 (English) 2004 National Institute of Standards and Technology. CODEN: ISDMAT. ISSN: 0147-1503. DOCUMENT TYPE: Journal CA Section: 68 (Phase Equilibriums, Chemical Equilibriums, and Solutions) The vapor pressures in the binary system were calcd. at T = 313.15 K. The smoothed pressure values are tabulated together with the mole fraction of 3-pentanol in the liq. and in the vapor phase. The std. deviations are also given. The exptl. data were reduced using the Wilson equation for the partial molar excess Gibbs energies.