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  2. Antoine equation - Wikipedia

    en.wikipedia.org/wiki/Antoine_equation

    The Antoine equation is a class of semi-empirical correlations describing the relation between vapor pressure and ... Ethanol 8.20417: 1642.89: 230.300: −57: 80 ...

  3. Vapor pressure - Wikipedia

    en.wikipedia.org/wiki/Vapor_pressure

    The Antoine equation [3] [4] is a pragmatic mathematical expression of the relation between the vapor pressure and the temperature of pure liquid or solid substances. It is obtained by curve-fitting and is adapted to the fact that vapor pressure is usually increasing and concave as a function of temperature. The basic form of the equation is:

  4. Non-random two-liquid model - Wikipedia

    en.wikipedia.org/wiki/Non-random_two-liquid_model

    VLE of the mixture of chloroform and methanol plus NRTL fit and extrapolation to different pressures. The non-random two-liquid model [1] (abbreviated NRTL model) is an activity coefficient model introduced by Renon and Prausnitz in 1968 that correlates the activity coefficients of a compound with its mole fractions in the liquid phase concerned.

  5. Dortmund Data Bank - Wikipedia

    en.wikipedia.org/wiki/Dortmund_Data_Bank

    The Dortmund Data Bank [1] (short DDB) is a factual data bank for thermodynamic and thermophysical data. Its main usage is the data supply for process simulation where experimental data are the basis for the design, analysis, synthesis, and optimization of chemical processes.

  6. Methanol (data page) - Wikipedia

    en.wikipedia.org/wiki/Methanol_(data_page)

    Here is a similar formula from the 67th edition of the CRC handbook. Note that the form of this formula as given is a fit to the Clausius–Clapeyron equation, which is a good theoretical starting point for calculating saturation vapor pressures: log 10 (P) = −(0.05223)a/T + b, where P is in mmHg, T is in kelvins, a = 38324, and b = 8.8017.

  7. Ethanol (data page) - Wikipedia

    en.wikipedia.org/wiki/Ethanol_(data_page)

    Phase behavior Triple point: 150 K (−123 °C), 0.00043 Pa Critical point: 514 K (241 °C), 63 bar Std enthalpy change of fusion, Δ fus H o +4.9 kJ/mol

  8. Ethyl cyanoacetate - Wikipedia

    en.wikipedia.org/wiki/Ethyl_cyanoacetate

    Vapour pressure of ethyl cyanoacetate. The vapor pressure follows the Antoine equation log 10 (P) = A−(B/(T+C)) (P in bar, T in K) with A = 7.46724, B = 3693.663 and C = 16.138 in the temperature range from 341 to 479 K [6] Two polymorphic forms occur.

  9. Hand boiler - Wikipedia

    en.wikipedia.org/wiki/Hand_boiler

    = the height of the column of fluid above the fluid's level in the lower bulb = the difference in vapor pressure between the two bulbs (which can be determined via the Antoine equation) = the density of the liquid