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### PETE 310

Lectures # 6 & # 7

Phase Behavior – Pure Substances (Lecture # 5)

Two Component Mixtures

Three & Multicomponent Mixtures

Learning Objectives

After completing this chapter you will be able to:

- Understand pure component phase behavior as a function of pressure, temperature, and molecular size.
- Understand the behavior of binary and multicomponent mixtures
- Behavior understood through proper interpretation of phase diagrams

Phase Diagrams

- Types of phase diagrams for a single component (pure substance)
- (PT)
- (PV) or (Pr)
- (TV) or (Tr)

Critical

2

phases

Point

P

c

Solid

Liquid

(1 phase)

(1 phase)

Pressure

Vapor Pressure

Curve (2 phases)

Vapor (1 phase)

Triple Point

(3 phases)

Sublimation Curve (2 phases)

T

Temperature

c

Phase DiagramsSingle Component Phase Diagram

Pure Component Properties

- Tabulated critical properties (McCain)

P

v

Lv

=

T

D

V

dT

Heat Effects Accompanying Phase Changes of Pure SubstancesClapeyron equation

Btu/lb-mol

With

DV = VMg-VMl

P

v

Lv

V

dT

Lv

d

P

v

P

v

dT

2

R

T

Heat Effects Accompanying Phase Changes of Pure Substances=

T

D

Approximate relation (Clausius - Clapeyron Equation)

=

Example of Heat Effects Accompanying Phase Changes

- Steam flooding Problem:

Calculate how many BTU/day (just from the latent heat of steam) are provided to a reservoir by injecting 6000 bbl/day of steam at 80% quality and at a T=462 oF

2

3

4

5

gas

gas

b

V

V

V

=

V

t1

t2

V

t3

t4

t5

V

liquid

liquid

liquid

liquid

liquid

Hg

Hg

Hg

Hg

Hg

>>

P

P

>

P

P

=

P

P

=

P

P

=P

P

1

s

2

s

3

s

4

s

5

s

Determination of Fluid PropertiesPs =saturation pressure

Temperature of Test Constant

Binary Mixtures

- Relationships to analyze: P, T, molar or specific volume or (molar or mass density) - as for a pure component –

+

- COMPOSITION – Molar Composition

Hydrocarbon Composition

- The hydrocarbon composition may be expressed on a weight basis or on a molar basis (most common)
- Recall

Hydrocarbon Composition

- By convention liquid compositions (mole fractions) are indicated with an x and gas compositions with a y.

Key Concepts

- Fraction of vapor (fv)
- Mole fractions in vapor (or gas) phase yi
- Mole fractions in liquid (or oil) phase xi
- Overall mole fractions (zi) combining gas & liquid

Binary Mixtures

- Types of phase diagrams for a two- component mixture
- Most common
- (PT) zi at a fixed composition
- (Pzi) T at a fixed T
- (Tzi) Pat a fixed P
- (PV) zi or (Pr) zi

CB

CP

Liquid

CT

Bubble Curve

Pressure

2 Phases

Gas

Dew Curve

Temperature

Pressure vsTemperature Diagram (PT)ziTa

Liquid

P1v

P1v

Bubble Curve

Pressure

2-phases

CP2

Dew Curve

P2v

Vapor

P2v

1

Ta

0

Temperature

x1, y1

Pressure Composition Diagrams - Binary SystemsTemperature vs. Composition Diagrams – Binary Systems

Pa

T2s

CP1

Dew Curve

Pressure

2-phases

CP2

Pa

Bubble Curve

T1s

T2s

Temperature

1

T1s

x1, y1

0

z

= fix

ed

1

T

= T

CP

a

B

M

P

B

C

Pressure

P

D

y

1

T

0

x

z

1

a

1

1

Temperature

Gas-Liquid Relationsz1=overall mole fraction of [1], y1=vapor mole fraction of [1], x1=liquid mole fraction of [1]

C1

C1

Gas

Gas

Gas

2-phase

2-phase

Liquid

Liquid

nC5

C3

nC5

C3

nC5

C3

p=500 psia

p=14.7 psia

p=380 psia

C1

C1

C1

Gas

Gas

2-phase

2-phase

Liquid

Liquid

Liquid

nC5

C3

nC5

nC5

p=2000 psia

p=2350 psia

p=1500 psia

Ternary Diagrams: ReviewPressure Effect

C3

C3

Ternary Diagrams: Review

Dilution Lines

Ternary Diagrams: Review

Quantitative Representation of Phase Equilibria - Tie (or equilibrium) lines

- Tie lines join equilibrium conditions of the gas and liquid at a given pressure and temperature.
- Dew point curve gives the gas composition.
- Bubble point curve gives the liquid composition.

Ternary Diagrams: Review

Quantitative Representation of Phase Equilibria - Tie (or equilibrium) lines

- All mixtures whose overall composition (zi) is along a tie line have the SAME equilibrium gas (yi) and liquid composition (xi), but the relative amounts on a molar basis of gas and liquid (fv and fl) change linearly (0 – vapor at B.P., 1 – liquid at B.P.).

Uses of Ternary Diagrams

Representation of Multi-Component Phase Behavior with a Pseudoternary Diagram

- Ternary diagrams may approximate phase behavior of multi-component mixtures by grouping them into 3 pseudocomponents
- heavy (C7+)
- intermediate (C2-C6)
- light (C1, CO2 , N2- C1, CO2-C2, ...)

Exercise

Find overall composition of mixture made with 100 moles oil "O" + 10 moles of mixture "A".

__________________________

________________________

_______________________

_____________________

___________________

_________________

P=200 psia

T=180F

P=14.7 psia

T=180F

P=600 psia

Pressure Effect

Pressure Effect

Pressure Effect

Pressure Effect

T=180F

P=400 psia

C1-C3-C10

O

O

O

O

Practice Ternary DiagramsPressure Effect

Pressure Effect

T=180F

P=4000 psia

T=180F

P=1000 psia

T=180F

P=2000 psia

T=180F

P=3000 psia

T=180F

P=1500 psia

O

O

O

O

O

Practice Ternary DiagramsPressure Effect

Temperature Effect

Temperature Effect

Temperature Effect

T=100F

P=2000 psia

T=200F

P=2000 psia

T=150F

P=2000 psia

T=300F

P=2000 psia

O

O

O

O

Practice Ternary DiagramsTemperature Effect

Temperature Effect

Temperature Effect

T=400F

P=2000 psia

T=450F

P=2000 psia

T=350F

P=2000 psia

O

O

O

Practice Ternary DiagramsTemperature Effect

1-Phase

CP

Bubble-Curve

60%

0%

Reservoir Pressure

20%

2-Phase

Dew-Curve

Reservoir Temperature

Pressure-Temperature Diagram for Multicomponent Systemst

1

Production

Production

t

2

2

Gas

Gas

Pressure

Injection

Injection

t

t

3

3

Temperature

Changes During Production and InjectionHomework

- See Syllabus please

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