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  • 8/9/2019 Oil Related Microbiology

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    Terje Torsvik

    UNI - CIPR

    CENTRE FOR INTEGRATED PETROLEUM RESEARCH

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    Important microbial processes in oil production:

    Microbial Influenced Corrosion (MIC)Produced water reinjection (PWRI)Microbial Enhanced Oil Recovery

    VFB

    VFA

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    pressure support

    Oxygen is removed to reduce corrosionSea water contains 28 mM sulphate

    Sea water injection promotes growth of SRB inthe water injection system and in thereservoir

    SRB use sulphate for respiration:

    4-

    2

    2 cause pro ems ecause s ox c an corros veTraditionally biocides have been used to inhibit SRBAn alternative method based on nitrate injection have been developed

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    H2S production increasesdramatically over thelifetime of a productionwell.

    High H 2S levels mayresu n s u own o ewell and reduced oil andgas production.

    H2S is toxic and

    corrosive

    Ref. : Sunde et al. 1993 . Field related mathematical

    Strong restrictions onH2S concentration in

    model to predict and reduce reservoir souring. SPE25197 (1993)

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    Laboratory experiments:Effect of nitrate injection on H2S production

    Sulphide production and nitrate injectin in column.

    1,2

    1,4

    mM H2S

    mM NO3

    0,4

    0,6

    0,8

    1,0

    m M

    H 2 S

    , N O 3 -

    0,0

    0,2

    100 300 500 700 900 1100

    Time (days)

    . . .

    model column. Appl. Microbiol Biotechnol 58: 400-408.

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    Gullfaks Water injection system Biofilm sampling

    Sampling point

    Sampling point

    Placed in box for anaerobic transportation

    Filled up with anaerobic injection sea water

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    Metal coupons incubated in pipeline

    Measuring microbial activityin the water injection system

    The biofilm is analyzed for microbial activity

    GAB NRBSRB

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    Water injection system at Gullfaks.

    1 0E+09

    1,0E+10

    1,0E+07

    1,0E+08

    2

    1,0E+04

    1,0E+05

    1,0E+06

    L o g c e

    l l s / c

    1 0E+01

    1,0E+021,0E+03

    1,0E+00

    f e b . 8 9

    j u n .

    9 0

    d e c .

    9 1

    m a r .

    9 3

    a p r .

    9 4

    n o v .

    9 4

    j u l . 9

    5

    j u n .

    9 6

    f e b . 9 7

    m a r .

    9 8

    m a y .

    9 9

    f e b . 0 0

    a u g . 0

    0

    m a y .

    0 1

    m a r .

    0 2

    f e b . 0 3

    Time (months)

    Biocide (glutaraldehyde) Nitrate (start oct. 99)

    -SRB-MPN

    NRBTotal bacteria

    Detect ion limit FA method: 1e+05 cells/cm2

    Detect ion limit MPN method: 6 cells/cm2

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    SRB activity and corrosion rate at GFB y ) Nitrate added

    e a r )

    1,0

    1,2

    H 2 S

    / c m

    2 / d

    20

    25

    r a t e ( m m

    /

    0,6

    0,8

    n r a

    t e ( g

    15

    C o r r o s i o n

    0,2

    0,4

    r e s p

    i r a t i o

    5

    10

    r . 9 4

    . 9 4

    . 9 4

    r . 9 5

    l . 9 5

    t . 9 5

    r . 9 6

    . 9 6

    . 9 6

    . 9 6

    . 9 7

    r . 9 7

    . 9 7

    . 9 7

    . 9 7

    . 9 8

    . 9 8

    r . 9 8

    . 9 8

    . 9 8

    . 9 8

    . 9 9

    . 9 9

    . 9 9

    . 0 0

    . 0 0

    . 0 0

    . 0 0

    . 0 0

    . 0 1

    . 0 1

    . 0 1

    . 0 1

    r . 0 2

    l . 0 2

    t . 0 2

    . 0 3

    . 0 3

    0,0

    S

    u l p h a

    t

    0

    Time (month)

    a p

    s e n o

    m a j o m

    a j u s e d e f e m

    a m a

    a u n

    o j a f e m a

    m a

    s e d e

    m a

    a u n

    o f e j u a u n

    o d e f e m

    a a u n

    o m a j o f e j u

    Corrosion rate

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    H2S in roduced water on Gullfaks C

    910

    678

    e w a t e r

    345

    g H

    2 S / l i t r

    measured mg H2S in water Theoretical H2S development

    12

    Start of nitrate injection

    nov-97 sep-98 jul-99 mai-00 feb-01 des-01 okt-02 aug-03

    Date

    Sunde, Egil; Lilleb, Bente-Lise Polden; Bdtker, Gunhild; Torsvik, Terje; Thorstenson, Tore. H2S inhibition by nitrateinjection on the Gullfaks field. NACE Corrosion 2004, Paper No 04760 ; 2004

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    Produced Water Reinjection (PWRI) has been used on platforms,

    mainly due to requirements from the Norwegian Pollution Agency

    In the event of permission to produce oil in the Barents Sea, theremust be zero release of h drocarbons to the environment.

    Challenges:High temperature stimulate growth of thermophilic SRBIncreased supply of VFA in the injected water stimulate reservoirsouring

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    Injection water:Cold sea water (StA)Hot produced water (StC)Microboal analysis of

    back flooded injectionwater

    Ocean floor

    Injection well Production well

    St A and B: Sea water

    Oil reservoir

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    Sam les Back-flooded injection water from wells 3000 meters below sea floor.

    of back-flooding.Sample Statfjord A Statfjord B Statfjord C

    Injected with Sea water Sea water Produced water

    Treatment Deoxygenated,biocide treatment

    Deoxygenated,nitrate treatment

    Deoxygenated,

    25 % seawater

    Souring potentialH2S mg/liter (calculated by Statoil)

    30

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    Principal component analysis of native populations at St A and C

    Statfjord A (StA)Statfjord C (StC)Produced water (PW)

    1 . 0 Thermoc

    StC

    Actinob

    Deferrib

    Backflowdelta

    StA

    betaFirmic

    PW

    - - 1 . 0

    alpha

    . .

    K. Lysnes, G. Bdtker, T. Torsvik, E. . Bjrnestad & Egil Sunde: Appl Microbio l Biotechnol (2009) 83:11431157

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    MEORPrinciples reservoir effects

    BACTERIA + OIL + N + P + O 2

    C E D

    L R E D U W P

    R

    E

    I N T E

    R F A

    T E N S

    I O

    E D

    E R

    R M E A B I L I T Y

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    Microbial biofilm on oil

    crude oil

    Bacterial colonysurrounded by water

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    - Best suited for low values (< 30 mN/m) Measurement range is 102 10-5 mN/m

    Method has been successfully applied down to 10-4 mN/m

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    Bacterum: Dietsia maris

    100

    Dodekan, aerobic synthetic sea water

    10

    OWB IFT

    4.0 ml/h

    0.9 ml/h1.8 ml/h

    0,1

    1

    I F T ( m N / m )

    2.7 ml/h

    5.4 ml/h

    0,01

    0,0010 2 4 6 8 10 12 14 16 18 20 22 24 26 28

    Run t ime (days)

    Kowalewski, E., Ruesltten, I., Gilje, E., Sunde, E., Bdtker, G., Lilleb, B.L.P., Torsvik, T., Stensen, J.., Bjrkvik, B." ", . ., , ,

    13th European Symposium on Improved Oil Recovery, Budapest, Hungary, Apr 25-27

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    Hopeman sandstone core

    45 cm long, 5 cm diameter Statfjord model oil

    a ora ory exper men sow ra e: , m m n =

    0,38Sor

    seawater

    Microbes O 2 N P

    0,36

    0,34

    0,32

    0 5 10 15 20

    Time (days)

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    MEOR at Norne

    Injection of aerobic seawater from start in

    1997

    MEOR implemented in January 2001 by

    stimulate bacterial growth in the reservoir

    Nitrate is also added in order to inhibit

    reservoir souring

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    2002: Increased oil production from MEOR at Norne

    900 000 m 3

    1 % of roducible oil

    At an oil price 20 $ per barrel and 1$= 5 NOK thisamounts to a roximatel 750 000 000 NOK.

    (Reported from Norne to OD in 2002)