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    PVT Short Course for Cairo UniversitySPE Student Chapter

    Ahmed Muaz

    Khalda Petroleum Company

    April 23, 2011

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    Contents

    Why Study PVT?

    Objectives of PVT Analysis

    Types of Reservoir Fluids

    Differentiation Between the Different Types

    of

    Reservoir Fluids

    Fluid Sampling

    Laboratory Experiments

    PVT Reports

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    Why Study PVT?

    Transport

    .Sep

    Gas

    StockTank

    Oil

    .Diff Flow Regime

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    Objectives of PVT Analysis

    Need to understand PVT analysis for:

    Determination of reservoir fluid type

    Knowledge of physical properties of reservoir fluids

    Match an EOS to the measured data

    Creation of PVT models

    Ultimate recoveries of different components

    Amounts and composition of liquids left behind

    Determination of well stream composition

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    Objectives of PVT Analysis Cont.

    Completion design

    Separator/NGL plant specifications

    Product values Vs. time

    Prediction compositional gradient

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    The Five Reservoir Fluids

    Black Volatile Retrograde Wet Dry

    Oil Oil Gas Gas Gas

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    Reservoir Fluid Type Identification

    Analyzing a representative sample in the lab

    Production data

    1.Initial GOR

    2.API

    3.Oil color

    4.C7+

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    Black Oil

    An initial GOR, 1750 SCF/STB or less

    A 45 API initial stock tank oil gravity or less

    A dark color of stock tank oil

    C7+ > 20 mole %

    Initial Bo of 2 res bbl/STB or less

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    Black Oil Phase Diagram

    T h e in itia l re se rvo ir

    ( & )con d ition s P T are

    m u ch lo w e r th a n

    th e critica l

    co n d itio n s

    T h e h e a vy m o le cu le s

    co n ce n tra tio n is

    h ig h

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    Volatile Oil

    An initial GOR, 1750 SCF/STB or greater

    A 51.2 API initial stock tank oil gravity

    A medium orange stock tank oil color

    C7+ concentration between 19 and 22 mole %

    Bo 2.0 res bbl/STB or greater

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    Volatile Oil Phase Diagram

    The initial reservoir

    conditions (P&T)

    are close to the

    critical conditions

    Have fewer heavy

    molecules than

    black oil

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    Retrograde Gas Condensate

    An initial GOR > 3200 SCF/STB

    API > 45 initial stock tank oil gravity

    A light stock tank oil color

    C7+ concentration

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    Retrograde Gas Phase Diagram

    The initial reservoir

    conditions (P&T) arehigher than thecritical conditions

    Have fewer heavy

    molecules thanvolatile oils

    The overallcomposition of the

    reservoir fluidbecomes heavier asthe lighter gas isproduced and theheavier condensate

    remains behind

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    Wet Gas

    An initial GOR > 15,000 SCF/STB

    API up to 70 initial stock tank oil gravity

    Water white of tank oil color

    C7+ concentration

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    Wet Gas Phase Diagram

    Reservoir

    Temperature aboveCricondentherm(pressure path notenter phaseenvelope)

    The reservoir fluid isgas throughout thelife of the reservoir

    The separatorcondition is twophases

    Gravity of stock tankliquid same as

    retrograde gas

    Temperature

    % Liquid

    2

    1

    ressure pathn reservoir

    e t g as

    Criticalpoint

    Bubble

    point

    line

    Separator

    150

    Dewp

    oint

    line

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    Dry Gas

    An initial GOR > 1000,000 SCF/STB

    Almost no liquid

    C7+ concentration < 0.7 mole %

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    Dry Gas Phase Diagram

    Primarily methane and

    some intermediates

    The reservoir fluid isgas throughout thelife of the reservoir

    No liquids formedeither in reservoir orat surface

    Temperature

    % Liquid

    2

    1

    ressure pathn reservoir

    r y g as

    Separator

    Dewp

    o in t

    l in e

    150

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    R e t r o g r a d ee t r o g r a d eR e g i o ne g i o n

    w o P h a s e R e g io nwo P h a s e R e g i o nTemperatureTemperature

    Pressur

    e

    Pressur

    e

    I LI L G A Slack Oil Volatile Critical Critical Gas Wet

    Oil Oil Gas

    Cricondenterm

    ew PointLociubblePointLoci

    r it ic al P oi ntricondenbar

    A

    B

    C

    eservoir Fluids Phase DiagramWindow

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    C7+ & GOR for Reservoir Fluids

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    Classification

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    Composition of Reservoir Fluids

    Differences Between Black and

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    Differences Between Black andVolatile Oil

    Black Oil

    The evolved gas is a dry gas.

    The solution gases remain gas phase in the

    reservoir, tubulars and separator.

    As reservoir pressure decreases, the gas leaving

    solution, becomes richer in intermediate

    components.

    API gradually decreases during the reservoir life.

    Phase Diagram of Black Oil and

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    Phase Diagram of Black Oil andAssociated Gas

    Production Processes for a Black

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    Production Processes for a BlackOil

    Differences Between Black and

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    Differences Between Black andVolatile Oil

    Volatile Oil

    The evolved gas is a retrograde gas.

    The evolved retrograde gases release a large

    amount of. condensate at surface conditions.

    Often over one half of the stock tank liquid produced

    during the reservoirs life.

    API steadily increases with time.

    Phase Diagram of Volatile Oil and

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    Phase Diagram of Volatile Oil andAssociated Gas

    Production Processes for a Volatile

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    Production Processes for a VolatileOil

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    Analysis and Prediction Tool

    Black Oil Mbal

    Assume free gas in the reservoir remains gas in the

    separator

    Treat a multi component black oil mixture as a two-

    component mixture: gas and oil

    Volatile Oil Mbal

    Treat mixture as a multi-component mixture

    Total composition of the production stream is known

    Effect of Using Black Oil Mbal for

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    Effect of Using Black Oil Mbal forVolatile Oil

    Differentiation between Volatile and

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    Differentiation between Volatile andRetrograde

    A G O R o f 3 2 0 0

    /S C F S TB is a g oo d

    -cu t o ff

    .A va lu e o f 1 2 5 m o le

    % +of C7 is a

    u se fu l d iv id in g lin e

    Differences between Volatile Oil

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    Differences between Volatile Oiland Retrograde Gas

    Retrograde Gas GOR increases with time as condensate dropout

    API increases with time

    Compositional Mbal should be used in reservoircalculations

    Conventional gas Mbal can be used above dew point

    Also, it can be used below dew point if two phase Z-

    factors are used

    Differences between Retrograde

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    Differences between Retrogradeand Wet Gas

    A n in itia l G O R o f

    , /1 5 0 0 0 S C F S T B

    ca n b e a cu to ff

    %A va lu e o f 4 m o le

    o r le ss ca n b e

    u se fu l d iv id in g lin e

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    of

    Reservoir Fluids

    R i Fl id S li

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    Reservoir Fluid Sampling

    Open Hole Sampling:

    RFT, small sample volume and often contaminated

    MDT, allows controlled drawdown and multiple

    sample chambers

    Optical MDT, allows to identify the type of fluid

    being sampled

    Cased Hole Sampling:

    Surface Sampling

    Subsurface Sampling

    f b f li

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    Surface & Subsurface Sampling

    W ll C di i i d i S li

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    Well Conditioning during Sampling

    Small perforation is preferable

    Limiting drawdown

    Large tubing diameter in case of high rates

    Better well cleaning

    Stable production

    No liquid slugging

    Small amount of produced fluid prior to sampling

    L b T

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    Laboratory Tests

    Primary tests

    Routine laboratory tests

    Special laboratory PVT tests

    P i T t

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    Primary Tests

    API

    Gas specific gravity

    Separator gas composition

    GOR

    Routine Laboratory Tests

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    Routine Laboratory Tests

    Constant-Composition Expansion - CCE

    Differential Liberation

    Constant-Volume Depletion CVD

    Separator Test

    Constant Composition Expansion -

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    Constant Composition Expansion CCE Test

    The test is conducted for the purposes of

    determining:

    Saturation pressure (bubble-point or dew-point

    pressure)

    Isothermal compressibility coefficients of the single-

    phase fluid in excess of saturation pressure

    Compressibility factors of the gas phase

    Total hydrocarbon volume as a function of pressure

    CCE T t P d

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    CCE Test Procedures

    GasLiquid

    Hg

    SecondStep

    Liquid

    Hg

    LiquidLiquid

    Hg

    FirstStep

    Hg

    ThirdStep

    Hg

    FourthStep

    Liquid

    GasVtLiquid

    Vt

    LiquidVtVt LiquidVt

    pb

    CCE Test Data

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    CCE Test Data

    Diff ti l Lib ti T t

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    Differential Liberation Test

    The experimental data obtained from the test

    include:

    Amount of gas in solution as a function of pressure

    The shrinkage in the oil volume as a function of

    pressure

    Properties of the evolved gas including the

    composition of the liberated gas, the gascompressibility factor, and the gas specific gravity

    Density of the remaining oil as a function of

    pressure

    erent a erat on xpans on est

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    Vo Liquid

    Hg

    Gas

    Hg

    Liquid

    Gas

    First step

    Hg

    Liquid

    GasLiquid

    Hg

    Vo

    Gas

    Vo

    Hg

    Liquid

    pb

    erent a erat on xpans on estProcedures

    Differential Liberation Test Data

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    Differential Liberation Test Data

    Separator Test Procedures

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    Separator Test Procedures

    LiquidHg

    Liquid

    Stocktank

    Gas

    Gas

    Liquid

    Se

    pa

    ra

    tor

    Hg

    pb

    resbbl

    STB

    resbbl

    STBBob =

    scf

    scf

    Rsb =scfSTB

    Separator Test Data

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    Separator Test Data

    CVD Test Procedures

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    CVD Test Procedures

    Constant Volume Depletion CVD

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    Co s a o u e ep e o CTest

    PVT Reports

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    PVT Reports

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    Thank You