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There can be VLE data for mixtures of four or more components, but such a boiling-point diagram is hard to show in either tabular or graphical form. For such multi-component mixtures, as well as binary mixtures, the vapor–liquid equilibrium data are represented in terms of K values (vapor–liquid distribution ratios) [1] [2] defined by
= the vapor–liquid equilibrium concentration of component in the liquid phase ( y / x ) {\displaystyle (y/x)} = Henry's law constant (also called the K value or vapor-liquid distribution ratio ) of a component
DePriester Charts provide an efficient method to find the vapor-liquid equilibrium ratios for different substances at different conditions of pressure and temperature. The original chart was put forth by C.L. DePriester in an article in Chemical Engineering Progress in 1953.
The table above gives properties of the vapor–liquid equilibrium of anhydrous ammonia at various temperatures. The second column is vapor pressure in kPa. The third column is the density of the liquid phase. The fourth column is the density of the vapor. The fifth column is the heat of vaporization needed to convert one gram of liquid to vapor.
The decrease in zero-point energy due to deuterium substitution will then be more important for R'–H than for R–H, and R'–D will be stabilized more than R–D, so that the equilibrium constant K D for R' + D–R ⇌ R'–D + R is greater than K H. This is summarized in the rule the heavier atom favors the stronger bond. [19]
The table below gives thermodynamic data of liquid CO 2 in equilibrium with its vapor at various temperatures. Heat content data, heat of vaporization, and entropy values are relative to the liquid state at 0 °C temperature and 3483 kPa pressure.
Dielectric constant, ... Vapor-liquid equilibrium for isopropanol/methanol [4] P = 101.325 kPa BP temp. °C % by mole methanol liquid vapor
Dielectric constant, ... Vapor-liquid Equilibrium for Ethyl Acetate/Water [3] P = 760 mmHg BP Temp. °C % by mole C 4 H 8 O 2; liquid vapor