Aga8 Versus Gerg2008

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    Measurement Data: from Well to Awarenesswww.SpiritIT.com

    GERG-2008 & AGA-8 UNCERTAINTY

    By Han van Dal

    [email protected]

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    UNCERTAINTY U95%

    SYSTEMATIC ERRORS (NOTICED OR UNNOTICED ?)

    Hardware failures

    Wrong setup / configuration

    Faulty data entries

    Fixed / frozen input values

    Wrong software version

    Power resets / reboots

    Proving / valve issues

    Sampling / lab analysis issues

    Failing As-found validations

    Calculation failures

    ...

    RANDOM ERRORS

    Measurement and analysis reproducibility

    Calibration uncertainty

    Lab analysis uncertainty

    Calculation uncertainty

    ...

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    GAS COMPRESSIBILITY EQUATIONS

    Natural gas compressibility = Real gas faktor

    = correction on ideal gas law

    1873 Van der Waals Equation Of State

    1940 Benedict Webb Rubin equation (BWR)

    (Soave) Redlich Kwong (SRK)

    Lee Kesser (LK)

    Peng Robinson (PR)

    1962 AGA NX-19

    1982 NX-19 PTB G9

    1991 S-GERG (AGA-8 Gross Method)

    1992 AGA-8 (AGA-8 Detailed Method)

    2004 GERG-2004 (later GERG-2008)

    Source : COMPRESSIBILITY OF NATURAL GAS - Jeffrey L. Savidge ISHM 2000

    Applies for AGA-8 Region 1

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    AGA-8 BOUNDARIES

    Source: AGA Transmission Measurement Committee Report No.8

    NX-19-40..+115C

    350 bar

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    OVERALL UNCERTAINTY WITH AGA-8 U95%= 0.1%

    Source: NFOGM 2003 'Handbook for uncertainty calculations Ultrasonic fiscal gas metering stations'

    NORWEGIAN SOCIETY FOR OIL AND GAS MEASUREMENT

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    http://www.nfogm.no/http://www.nfogm.no/
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    OVERALL UNCERTAINTY WITH AGA-8

    DETAILED INPUT LEVEL

    Relative Relative

    Given Relative Confidence Level Type of Standard Sensitivity Relative

    Input variables Uncertainty (probability distr.) Uncertainty Uncertainty Coefficient Variance

    MODEL UNCERTAINTY1)

    Gas compressibility factor at l ine conditions (Z) 0.1 % 95 % (normal) A 0.05000 % 1 0.00000025

    Gas compressibility factor at s tandard conditions (Z0) 0.052 % 95 % (normal) A 0.02600 % 1 6.76E-08

    ANALYSIS UNCERTAINTY

    Line conditions 0.16 % Standard A 0.16000 %

    1 0.00000256

    Standard conditions 0 % Standard A 0.00000 %

    Gas compressibility calculation Sum of relative variances, (EZ0/Z)2

    2.8776E-06

    Relative Combined Standard Uncertainty, E Z0/Z 0.001696

    Relative Expanded Uncertainty (95% c onfidence level, k=2), k EZ0/Z 0.3393 %

    1) Re. model uncertainty: AGA-8 uncertainty used for the model uncertainty of Z (line conditions)

    ISO 6976 uncertainty used for the model uncertainty of Z0 (standard reference conditions)

    Z at line conditions: Fill in AGA-8 uncertainty (option)

    Z at std. conditions: Fill in AGA-8 uncertainty (option) Z at std. conditions: Fill in ISO 6976 uncertainty (option)

    EMU - USM Fiscal Gas Metering Station

    Gas compressibility uncertainty

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    0.3

    Source: NFOGM 2003 'Handbook for uncertainty calculations Ultrasonic fiscal gas metering stations'

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    OVERALL UNCERTAINTY WITH AGA-8 U95%= 0.3%

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    Source: NFOGM 2003 'Handbook for uncertainty calculations Ultrasonic fiscal gas metering stations

    www.nfogm.no section Handbookshttp://gasmetering.azurewebsites.net

    http://www.nfogm.no/http://www.nfogm.no/http://gasmetering.azurewebsites.net/http://gasmetering.azurewebsites.net/http://gasmetering.azurewebsites.net/http://gasmetering.azurewebsites.net/http://www.nfogm.no/
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    AGA-8 UNCERTAINTY

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    Source: AGA Transmission Measurement Committee Report No.8

    Uncertainty = ? %

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    AGA-8 UNCERTAINTY

    Optimized for pipeline quality natural gas in Region 1

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    0.2 .. 0.5%

    GERG-2008 UNCERTAINTY

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    Source: AGA Transmission Measurement Committee Report No.8

    0.1%

    0.1% -183 .. + 177 C Up to 35 Mpa

    0.2 .. 0.5% -213 .. + 427 C Up to 70 Mpa

    No limits on composition

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    AGA-8 / GERG-2008 : DRY GAS

    Methane

    83.18

    Nitrogen

    9.94

    Carbon Dioxide

    1.79

    Ethane

    4.05

    Propane

    0.71

    Water 0.00

    Hydrogen Sulphide 0.00

    Hydrogen

    0.00

    Carbon Monoxyde 0.00

    Oxygen 0.00

    i-Butane

    0.00

    n-Butane

    0.23

    i-Pentane

    0.00

    n-Pentane

    0.05

    n-Hexane

    0.05

    n-Heptane 0.00

    n-Octane

    0.00

    n-Nonane 0.00

    n-Decane 0.00

    Helium

    0.00

    Argon 0.00

    NeoPentane 0.00

    Sum 100.00

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    Relative difference

    Z(AGA-8) Z(GERG2008)

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    AGA-8 / GERG-2008 : DRY GAS

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    AGA-8 / GERG-2008 : SEPARATOR GAS

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    Pressure bar(a)

    85

    Temperature C

    24

    Total

    Liquid

    Vapour

    C1

    mol frac.

    0.7302

    0.3837

    0.8673

    C2

    0.0786

    0.0884

    0.0748

    C3

    0.0431

    0.0834

    0.0271

    nC4

    0.0181

    0.0472

    0.0066

    iC4

    0.0326

    0.0764

    0.0153

    nC5

    0.0117

    0.0360

    0.0021

    iC5

    0.0166

    0.0470

    0.0045

    nC6

    0.0106

    0.0353

    0.0009

    nC7

    0.0209

    0.0713

    0.0009

    nC8

    0.0161

    0.0559

    0.0003

    nC9

    0.0118

    0.0412

    0.0001

    nC10

    0.0097

    0.0342

    0.0000

    Fraction

    mol frac.

    1.0000

    0.2835

    0.7165

    Fraction

    mass frac.

    1.0000

    0.5174

    0.4826

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    AGA-8 / GERG-2008 : SEPARATOR GAS

    Methane

    83.18

    Nitrogen

    9.94

    Carbon Dioxide

    1.79

    Ethane

    4.05

    Propane

    0.71

    Water

    0.00

    Hydrogen Sulphide 0.00

    Hydrogen 0.00

    Carbon Monoxyde

    0.00

    Oxygen 0.00

    i-Butane

    0.00

    n-Butane

    0.23i-Pentane

    0.00

    n-Pentane

    0.05

    n-Hexane

    0.05

    n-Heptane 0.00

    n-Octane 0.00

    n-Nonane

    0.00

    n-Decane

    0.00

    Helium 0.00

    Argon

    0.00

    NeoPentane 0.00

    Sum 100.00

    Relative difference

    Z(AGA-8) Z(GERG2008)

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    AGA-8 / GERG-2008 : SEPARATOR GAS

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    AGA-8 / GERG-2008 : SEPARATOR GAS

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    AGA-8 / GERG-2008 : WITH WATER

    Methane

    82.6

    Nitrogen

    0.32

    Carbon Dioxide

    2.01

    Ethane

    7.41

    Propane

    4.37

    Water

    0.5

    Hydrogen Sulphide

    0

    Hydrogen

    0

    Carbon Monoxyde

    0

    Oxygen

    0

    i-Butane

    0.83

    n-Butane

    1.07

    i-Pentane

    0.31

    n-Pentane

    0.25

    n-Hexane

    0.3

    n-Heptane

    0

    n-Octane

    0

    n-Nonane

    0

    n-Decane

    0

    Helium

    0.03

    Argon

    0

    NeoPentane

    0

    Sum

    100.00

    Relative difference

    Z(AGA-8) Z(GERG2008)

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    AGA-8 / GERG-2008 : WITH WATER

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    AGA-8 / GERG-2008 : WITH WATER

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    CONCLUSIONS

    AGA-8 IS ACCURATE FOR DRY GAS

    as accurate as GERG-2008

    also accurate in expanded range

    AGA-8 IS LESS SUITED FOR WET GAS

    (BOTH HC AND H2O)

    calculation failures

    increased uncertainty

    GERG-2008 IS ACCURATE AND ROBUST

    0.1% for both dry and wet gases

    no limitation on composition

    no calculation failures

    10 x CPU time of AGA-8

    GERG2008 ALSO FOR LIQUID ?!

    liquid density U95= 0.1 .. 0.5 %

    online comparison with Coriolis density to

    verify well composition ?!

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    Measurement Data: from Well to Awarenesswww.SpiritIT.com

    THANK YOU FOR YOUR ATTENTION

    Questions?