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Phase Behavior and ThermodynamicsPVT Properties

Liquid-Phase Component Mole Fraction Formula

x=zL+VKx=\frac{z}{L+VK}

Liquid-Phase Component Mole Fraction calculates liquid-phase mole fraction for pvt properties workflows in phase behavior and thermodynamics.

Calculate

How engineers use this formula

Use this formula when the listed inputs (z, L, V, K) are known and the assumptions behind the cited pvt properties relationship match the engineering case being checked.

Assumptions

  • Input values are representative for the well, reservoir, fluid, or equipment case being evaluated.
  • The declared units match the field-unit constants used in the formula.
  • The cited formula applies to the selected petroleum engineering workflow.

Limitations

  • The calculation does not replace a full engineering model or operating procedure.
  • Accuracy depends on the source correlation, assumptions, input quality, and unit consistency.

Common mistakes

  • Mixing unit systems without converting the inputs.
  • Using default example values as field recommendations.
  • Applying the formula outside the source assumptions.

Default example

Using the default inputs, x equals 0.208333 fraction.

zfraction

0.25

Lmol/mol feed

0.6

Vmol/mol feed

0.4

Kdimensionless

1.5

Inputs

z

fraction

Feed Mole Fraction of Component

L

mol/mol feed

Liquid Leaving per Mole Feed

V

mol/mol feed

Vapor Leaving per Mole Feed

K

dimensionless

Equilibrium Vaporization Ratio

Outputs

x

fraction

Liquid-Phase Mole Fraction

z

fraction

Feed Mole Fraction of Component

L

mol/mol feed

Liquid Leaving per Mole Feed

V

mol/mol feed

Vapor Leaving per Mole Feed

K

dimensionless

Equilibrium Vaporization Ratio

Source and review

reviewed

Gas Conditioning and Processing, Campbell, J. M. (1992)

John M. Campbell. 1992. Gas Conditioning and Processing, Campbell Petroleum Series, Vol. 1, Page 107.

Source

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