Vapour pressures of common liquids

Saturated vapour pressures of diethyl ether, acetone, ethanol, water and toluene at several temperatures, with their normal boiling points and enthalpies of vaporization. The vapour-pressure curves and boiling-point–altitude relations on this site are computed from these equations.

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Diethyl ether(CX2HX5)X2O\ce{(C2H5)2O}24.7971.43170.834.5026.52A=4.13377, B=1102.878, C=-40.46 (212.4–330 K)
AcetoneCHX3COCHX3\ce{CH3COCH3}9.4030.6081.456.0529.10A=4.42448, B=1312.253, C=-32.445 (259.16–507.6 K)
EthanolCX2HX5OH\ce{C2H5OH}1.597.8929.478.2938.56A=5.37229, B=1670.409, C=-40.191 (273–351.7 K); A=5.24677, B=1598.673, C=-46.424 (351.7–366.63 K)
WaterHX2O\ce{H2O}0.613.1712.499.9740.65IAPWS-IF97
TolueneCX6HX5CHX3\ce{C6H5CH3}0.913.8112.3110.6333.18A=4.23679, B=1426.448, C=-45.957 (273.13–303 K); A=4.07827, B=1343.943, C=-53.773 (303–384.66 K)

The ether fit was made for 212–293 K and is extended here to 330 K, where it is within about 0.2 K at the normal boiling point; ethanol and toluene at 0 °C are slight extrapolations.

Sources

  1. NIST Chemistry WebBook, SRD 69: Antoine parameters, log10(p/bar) = A − B/(T/K + C) (ethanol: Kretschmer & Wiebe 1949, Ambrose & Sprake 1970; acetone: Ambrose et al. 1974; diethyl ether: Taylor & Smith 1922; toluene: Besley & Bottomley 1974, Williamham et al. 1945).
  2. IAPWS-IF97 region-4 saturation equations (water).
  3. W. M. Haynes (ed.), CRC Handbook of Chemistry and Physics, 97th ed. (2016): normal boiling points and enthalpies of vaporization.

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