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1
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- Chapter 12
- Gas-Liquid Equilibrium
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2
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- Applications to low pressures
- Simplifications
- the gas phase behaves as an Ideal Gas
- the liquid phase exhibits Ideal Solution Behavior
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3
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- The equilibrium criteria between 2 phases a and b is,
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4
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- The last criteria implies “tendency of a component to be in phase a or b
is balanced” – “net mass transfer across phases is zero”
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5
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- Gas phase behaves as an ideal gas (IG), and liquid phase behaves as an
ideal solution (IS).
- These assumptions imply that
- IG: molecular interactions are zero, molecules have no volume.
- IS: forces of attraction/repulsion between molecules are the same
regardless of molecular species. Volumes are additive (Amagat’s Law).
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6
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7
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8
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9
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- By convention liquid compositions (mole fractions) are indicated with an
x and gas compositions with a y.
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10
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11
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- Isothermal Reservoir Depletion Process for a
- Reservoir Oil with 2 Components
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12
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13
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- The bubble point pressure at a given T is
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14
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15
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- Under Raoult’s law, the bubble point has a linear dependence with the
vapor pressures of the pure components.
- Once the bubble point pressure is found, the equilibrium vapor
compositions are found from Raoult’s law.
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16
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- At the dew point the overall fluid composition coincides with the gas
composition. That is.
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17
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- Find DP pressure and equilibrium liquid compositions
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18
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19
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- In this type of calculations the objective is to:
- find fraction of vapor vaporized (fv) and equilibrium gas and liquid
compositions
- given the overall mixture composition, P and T.
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20
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- Start with the equilibrium equation
- Material balance
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21
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- Now replace either liquid or gas compositions using equilibrium equation
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22
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- Rearrange and sum over all yi
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23
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24
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- Objective function (flash function) is
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25
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- There are several equivalent expressions for the flash function
- (a)
- (b)
- (c)
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26
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- Once fv is found the equilibrium gas and liquid compositions
are evaluated from
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27
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- 1. Constants depend upon the component – Different Units
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28
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