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  2. Critical point (thermodynamics) - Wikipedia

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

    The commonly known phases solid, liquid and vapor are separated by phase boundaries, i.e. pressure–temperature combinations where two phases can coexist. At the triple point, all three phases can coexist. However, the liquidvapor boundary terminates in an endpoint at some critical temperature T c and critical pressure p c. This is the ...

  3. 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: ...

  4. Supercritical fluid - Wikipedia

    en.wikipedia.org/wiki/Supercritical_fluid

    As the critical temperature is approached (300 K), the density of the gas at equilibrium becomes higher, and that of the liquid lower. At the critical point, (304.1 K and 7.38 MPa (73.8 bar)), there is no difference in density, and the 2 phases become one fluid phase. Thus, above the critical temperature a gas cannot be liquefied by pressure.

  5. Phase diagram - Wikipedia

    en.wikipedia.org/wiki/Phase_diagram

    The equilibrium conditions are shown as curves on a curved surface in 3D with areas for solid, liquid, and vapor phases and areas where solid and liquid, solid and vapor, or liquid and vapor coexist in equilibrium. A line on the surface called a triple line is where solid, liquid and vapor can all coexist in equilibrium. The critical point ...

  6. Saturation dome - Wikipedia

    en.wikipedia.org/wiki/Saturation_Dome

    The point at the very top of the dome is called the critical point. This point is where the saturated liquid and saturated vapor lines meet. Past this point, it is impossible for a liquidvapor transformation to occur. [3] It is also where the critical temperature and critical pressure meet.

  7. Cubic equations of state - Wikipedia

    en.wikipedia.org/wiki/Cubic_equations_of_state

    The model should provide reasonable accuracy near the critical point, particularly for calculations of the compressibility factor and liquid density. The mixing rules should not employ more than a single binary interaction parameter, which should be independent of temperature, pressure, and composition.

  8. 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 ...

  9. Maxwell construction - Wikipedia

    en.wikipedia.org/wiki/Maxwell_construction

    Experiments show that if the volume of a vessel containing a fixed amount of liquid is heated and expands at constant temperature, at a certain pressure, (), vapor, (denoted by dots at points and in Fig. 1) bubbles nucleate so the fluid is no longer homogeneous, but rather it has become a heterogeneous mixture of boiling liquid and condensing ...