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  2. Volume correction factor - Wikipedia

    en.wikipedia.org/wiki/Volume_Correction_Factor

    That is, observed temperatures above 60 °F (or the base temperature used) typically correlate with a correction factor below "1", while temperatures below 60 °F correlate with a factor above "1". This concept lies in the basis for the kinetic theory of matter and thermal expansion of matter , which states as the temperature of a substance ...

  3. UNIFAC - Wikipedia

    en.wikipedia.org/wiki/UNIFAC

    By adding a correction factor, known as the activity (, the activity of the i th component) to the liquid phase fraction of a liquid mixture, some of the effects of the real solution can be accounted for. The activity of a real chemical is a function of the thermodynamic state of the system, i.e. temperature and pressure.

  4. Fenske equation - Wikipedia

    en.wikipedia.org/wiki/Fenske_equation

    Fractionation at total reflux. The Fenske equation in continuous fractional distillation is an equation used for calculating the minimum number of theoretical plates required for the separation of a binary feed stream by a fractionation column that is being operated at total reflux (i.e., which means that no overhead product distillate is being withdrawn from the column).

  5. Modeling and simulation of batch distillation unit - Wikipedia

    en.wikipedia.org/wiki/Modeling_and_simulation_of...

    Specifying input stream information that is temperature, pressure, Composition type and flow rate of the components; Temperature = 373 K, Pressure=1 bar Flow basis = Volume( 50 L/hr) Composition type = mole fraction Ethanol - 0.5, Water – 0.5 Specifying block information what type of distillation column is present (Pot +overhead condenser type)

  6. NTU method - Wikipedia

    en.wikipedia.org/wiki/NTU_Method

    The number of transfer units (NTU) method is used to calculate the rate of heat transfer in heat exchangers (especially parallel flow, counter current, and cross-flow exchangers) when there is insufficient information to calculate the log mean temperature difference (LMTD). Alternatively, this method is useful for determining the expected heat ...

  7. UNIQUAC - Wikipedia

    en.wikipedia.org/wiki/UNIQUAC

    This eliminates the use of experimental data to calculate the UNIQUAC parameters, [3] extensions for the estimation of activity coefficients for electrolytic mixtures, [7] extensions for better describing the temperature dependence of activity coefficients, [8] and solutions for specific molecular arrangements.

  8. Gravity (alcoholic beverage) - Wikipedia

    en.wikipedia.org/wiki/Gravity_(alcoholic_beverage)

    The ratio depends on the temperature and pressure of both the sample and water. The pressure is always considered (in brewing) to be 1 standard atmosphere (1,013.25 hPa) and the temperature is usually 20 °C (68 °F) for both sample and water but in some parts of the world different temperatures may be used and there are hydrometers sold ...

  9. Theoretical plate - Wikipedia

    en.wikipedia.org/wiki/Theoretical_plate

    The calculation process requires the availability of a great deal of vapor–liquid equilibrium data for the components present in the distillation feed, and the calculation procedure is very complex. [2] [3] In an industrial distillation column, the N t required to achieve a given separation also depends upon the amount of reflux used. Using ...