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Lecture11b_Basic Gaslift Sec 2 - Hardware

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  • 7/28/2019 Lecture11b_Basic Gaslift Sec 2 - Hardware

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    Gas Lift

    COMPRESSION STATION

    GAS LIFTED

    WELL EXPORT LINEGAS/OIL

    BORE

    SEPARATORPROCESS

    WEL

    L

    NEAR WELLBORESURFACE FACILITIES

    Slide 2Section 2 - Hardware

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    Gas Lift

    Gas lift System

    Low Pressure gas Liftgas

    Produced Fluids + Lif t Gas

    High Pressure Gas

    up the well,

    lightening

    the fluid

    GasliftCompressor

    eparator

    Liquid

    the well

    Lift gas

    injected at

    mandrel

    Pwf

    Slide 3Section 2 - Hardware

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    Gas Lift

    Tubing, Casing, Packer,

    High

    Pressure Lift

    Gas

    Produced Fluids + Lift Gas

    UnloadinMandrels and Gas Lift

    valves

    Tubing

    valves

    (Closed

    after

    Unloadin

    inside the mandrels andthe mandrels is part of the

    tubin

    Casing/Tubin

    g AnnulusOperating

    Valve

    (Always

    Upper valves are for

    unloading

    Packer

    open)

    Bottom valve is foroperationPerforationsReservoir

    Slide 4Section 2 - Hardware

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    Gas Lift

    5 1/2 MMRG-4, 1 1/2 POCKET

    ROUND MANDREL DESIGN CAMCO

    OrientingSleeve

    ToolDiscriminator

    G LatchLug

    PolishedSeal Bore

    ENGINEERING DATA

    PART NUMBER 05712-000-00001

    SIZE 5 1/2. . .

    MIN I.D. 4.756

    DRIFT I.D. 4.653THREAD 17 LB/FT MANN BDS B x P

    TEST PRESSURE INTERNAL 7740 PSI

    LATCH TYPE RK, RK-1, RKP, RK-SPKICKOVER TOOL OM-1, OM-1M, OM-1SRUNNING TOOL RK-1 15079PULLING TOOL 1 5/8 JDS 15155

    MATERIAL 410 S.S., 13 CR 22 HRC MAX

    Slide 5Section 2 - Hardware

    TENSILE STRENGTH (EOEC) 490,000 LBS

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    Gas Lift

    CAMCO

    Slide 6Section 2 - Hardware

    ..

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    Gas Lift

    Gas lift Valve Features

    Bellows protection

    Max dome char e

    Check valve Stem travel

    Elastomers

    Max fluid rate

    Slide 7Section 2 - Hardware

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    Gas Lift

    IPO G/L Valve Com onents

    Check valve to hold

    Dome area which

    holds nitrogen

    Valve bellows. Grows

    in length with

    pressure charge

    .

    Valve stem with ball

    tip

    Check valve. Seats

    Valve choke

    w en u ve oc y s

    in upward direction.

    Slide 8Section 2 - Hardware

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    Gas Lift

    Gaslift Valve Installation

    A as lift valve is run and

    pulled with a special

    kickover pulling tool

    Slide 9Section 2 - Hardware

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    Gas Lift

    T e of Gas Lift Valves

    3 basic types of gas li ft valves, each available in 1 & 1-1/2

    sizes:

    Dummy Orifice Unloadingva ves va ves va ves

    (DKO-2) Venturi (nova)

    operated valve (BK-1) production pressure

    (BKR-5, RF-1)

    Throttling/proportional-

    Combination valve

    Slide 10Section 2 - Hardware

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    Gas Lift

    IPO Valve

    Advantages

    Flexible to uncertainty of well data

    Re-opening of unloading valves can be avoided

    Requires higher injection pressure

    Field personnel need to intervene once the well isunloaded and flowing to reduce injection pressure to

    close the unloading valves

    , , .need to readjust injection gas

    Slide 11Section 2 - Hardware

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    Gas Lift

    PPO Valve

    e common y use ype o gas va ve n uacompletion wells is Production Pressure Operated

    Gaslift Valve (PPO) vantage

    Utilizes full injection pressure at operating valve depth

    Deeper injection depth

    Little attention by field personnel Disadvantage

    More mandrels/Valves needed than ressure o erateddesign

    Needs accurate well data.

    Increase in Water Cut/FTHP can cause the shallowervalves to re-open

    Slide 12Section 2 - Hardware

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    Gas Lift

    Pb

    Dome

    ChevronPacking

    Normally required during

    unloading phase only

    Bellows

    Stack pen on y w en u ng anannulus pressures are high

    Pc

    Stem Tip (Ball)

    Square EdgedSeat

    setting pressure

    Valve closes after transfer toPt

    ChevronPackingStack

    next station

    May be spring or nitrogenCheck Valve

    Production Pressure

    operated gas lift valve

    charged

    Slide 13Section 2 - Hardware

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    Gas Lift

    If Pupstream > Pset, valve opens and maintains Upsteram Pressure = Pset

    Diaphragm/Atmospheric Bellows

    Spring

    Stem

    Stem Tip

    DownstreamUpstream

    Pressure Regulator

    Slide 14Section 2 - Hardware

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    Gas Lift

    Diaphragm/Atmospheric Bellows

    Spring

    Stem

    Stem Tip

    Upstream

    /Casing

    DownstreamUpstream

    Pressure Regulator

    S rin O erated Gas Lift Valve

    Downstream / Tubing

    Slide 15Section 2 - Hardware

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    Gas Lift

    Large sub-critical flow regime

    Gas passage dependentThe Square-edged120120140140

    160160

    180180

    (MCF/d)

    e(MCF/d)

    on downstream pressure

    until 40 - 50% pressure

    lost

    orifice performance

    curve

    2020

    4040

    6060

    8080

    100100

    Flow

    Rat

    Flow

    Rat

    Poor pressure recovery= large pressure drop &

    0000 100100 200200 300300 400400 500500 600600

    Tubing PressureTubing PressureTubing Pressure

    large energy loss

    Slide 17Section 2 - Hardware

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    Gas Lift

    Plot of Gas Rate Versus Pressure

    SUB-CRITICALORIFICE FLOWSC

    F/D)

    RATE(M

    NJECTION

    GASI

    PTUBING = 55%

    Slide 18Section 2 - Hardware

    CASING

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    Gas Lift

    Nova Valve

    Venturi Valve (orif ice type)

    always open - allows gas passage whenever correctdifferential exists

    Achieved critical flow with Delta P of 100 psi

    Gas injection controlled by size and differential across

    replaceable choke Check valve prevents reverse flow of well fluids from the

    production conduit

    Slide 19Section 2 - Hardware

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    Gas Lift

    O eratin Princi les of the Venturi THE VENTURI DESIGN ALLOWS THE FOLLOWING :

    BETTER PRESSURE & ENERGY RECOVERY

    DRASTICALLY REDUCED SUB-CRITICAL FLOW REGIME

    CRITICAL VELOCITY (VELOCITY OF PRESSURE TRANSMISSION/SONIC

    VELOCITY) ATTAINED WITHIN 10% PRESSURE DROP

    Nozzle-Venturi Gas Lift Valve ProjectNozzle-Venturi Gas Lift Valve ProjectNozzle-Venturi Gas Lift Valve Project

    REDUCES INFLUENCE OF DOWNSTREAM PRESSURE ON GAS PASSAGE =REDUCED RISK TO PROPAGATING INSTABILITY

    Pressure vs. F ow Rate SummaryPressure vs. F ow Rate Summaryressure vs. ow ae ummary

    300030003000

    350035003500

    400040004000

    1400 psi Upstream1400 psi Upstream

    /d)/d)

    150015001500

    200020002000

    250025002500

    Conventional Orifice ValveConventional Orifice Valve

    Improved Orifice ValveImproved Orifice Valve

    w

    Rate

    (Mcf

    w

    Rate

    (Mc

    900 psi Upstream900 psi Upstream

    000

    500500500

    100010001000

    0 200 400 600 800 1000 120 1400

    400 psi Upstream400 psi UpstreamFlFl

    Slide 20Section 2 - Hardware

    Downstream Pressure (psi)Downstream Pressure (psi)Data shown is from actual flow testsData shown is from actual flow tests

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    Gas Lift

    Nova Versus S uare Ed e Orifice

    /D)

    SUB-CRITICAL

    FLOW

    CRITICAL FLOW

    E(

    MMSC

    CRITICAL FLOW

    TIONRA

    ASINJ

    E

    PRESSURE (PSI) PCASING

    PTUBING = 90%PTUBING = 55%

    Slide 21Section 2 - Hardware


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