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  2. Critical point (thermodynamics) - Wikipedia

    en.wikipedia.org/wiki/Critical_point...

    The liquidliquid critical point of a solution, which occurs at the critical solution temperature, occurs at the limit of the two-phase region of the phase diagram. In other words, it is the point at which an infinitesimal change in some thermodynamic variable (such as temperature or pressure) leads to separation of the mixture into two ...

  3. Supercritical liquid–gas boundaries - Wikipedia

    en.wikipedia.org/wiki/Supercritical_liquid–gas...

    However, different criteria still allow to distinguish liquid-like and more gas-like states of a supercritical fluid. These criteria result in different boundaries in the pT plane. These lines emanate either from the critical point, or from the liquidvapor boundary (boiling curve) somewhat below the critical point.

  4. Propane (data page) - Wikipedia

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

    Critical point: 369.522 K (96.672 °C), 42.4924 bar ... Liquid properties Std enthalpy change of formation, ... log of propane vapor pressure. Uses formula: ...

  5. Phase diagram - Wikipedia

    en.wikipedia.org/wiki/Phase_diagram

    Boiling-point diagram. A two component diagram with components A and B in an "ideal" solution is shown. The construction of a liquid vapor phase diagram assumes an ideal liquid solution obeying Raoult's law and an ideal gas mixture obeying Dalton's law of partial pressure. A tie line from the liquid to the gas at constant pressure would ...

  6. Supercritical fluid - Wikipedia

    en.wikipedia.org/wiki/Supercritical_fluid

    In the pressure-temperature phase diagram (Fig. 1) the boiling curve separates the gas and liquid region and ends in the critical point, where the liquid and gas phases disappear to become a single supercritical phase. The appearance of a single phase can also be observed in the density-pressure phase diagram for carbon dioxide (Fig. 2).

  7. Redlich–Kwong equation of state - Wikipedia

    en.wikipedia.org/wiki/Redlich–Kwong_equation_of...

    It soon became desirable to obtain an equation that would also model well the Vaporliquid equilibrium (VLE) properties of fluids, in addition to the vapor-phase properties. [10] Perhaps the best known application of the Redlich–Kwong equation was in calculating gas fugacities of hydrocarbon mixtures, which it does well, that was then used ...

  8. Saturation dome - Wikipedia

    en.wikipedia.org/wiki/Saturation_Dome

    A saturation dome uses the projection of a P–v–T diagram (pressure, specific volume, and temperature) onto the P–v plane. The points that create the left-hand side of the dome represent the saturated liquid states, while the points on the right-hand side represent the saturated vapor states (commonly referred to as the “dry” region).

  9. Maxwell construction - Wikipedia

    en.wikipedia.org/wiki/Maxwell_construction

    This violation is not a defect, rather it is the origin of the observed discontinuity in properties that distinguish liquid from vapor, and defines a first order phase transition. Figure 1: The curve is an isotherm, constant, in the --plane of a fluid that includes a phase change. The various segments of the curve are described in the text.

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