36
코렐테크놀로지㈜ 기술경영연구소장 이선엽 Highway Bridges $8 3 부식비용 cost of corrosion Highway Bridges Gas and Liquid Transm. Pipelines Waterways and Ports Hazardous Materials Storage Ai P t $8.3 $7.0 $0.3 $7.0 미국의 부식비용: 총 2,2760억불 상수도시스템 Air Ports Railroads Gas Distribution - - $5.0 Drinking Water and Sewer System $36 0 이중 상수도시스템부식비용: 360억불 (2003년 기준) Electrical Utilities Telecommunication Motor Vehicles $6.9 - $23.4 Drinking Water and Sewer System $36.0 Ships Aircraft Railroad Cars Hazardous Materials Transport $2.7 $2.2 $0.5 $0 9 Hazardous Materials Transport Oil and Gas Expl. And Production Mining Petroleum Refining $0.9 $1.4 $3.7 $0.1 Report No. FHWA-RD-01-156 “Corrosion Cost and Preventive Strategies in the United States”, GerhardusH. Koch, M.P.H. Brongers, N.G. Thompson, Y.P. Virmani, J.H. Payer, Office of Infrastructure Research and Development Federal Chem., Petrochem., Parm. Pulp and Paper Agricultural Food Processing $1.7 $6.0 $1.1 $2.1 Payer, Office of Infrastructure Research and Development Federal Highway Administration, Department of Transportation, 2003 Electronics Home Appliances Defense N l W t St - $1.5 $20.0 $0 1 Nuclear Waste Storage $0.1 Cost of Corrosion Per Analyzed Economic Sector, ($ x billion) $10 $20 $30 $0 $40

현장적용기술-이선엽

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  • Highway Bridges $8 3

    cost of corrosionHighway Bridges

    Gas and Liquid Transm. PipelinesWaterways and Ports

    Hazardous Materials StorageAi P t

    $8.3$7.0

    $0.3$7.0 : 2,2760

    Air PortsRailroads

    Gas Distribution

    --

    $5.0Drinking Water and Sewer System $36 0

    : 360(2003 )

    Electrical UtilitiesTelecommunication

    Motor Vehicles

    $6.9-

    $23.4

    Drinking Water and Sewer System $36.0

    ShipsAircraft

    Railroad CarsHazardous Materials Transport

    $2.7$2.2

    $0.5$0 9Hazardous Materials Transport

    Oil and Gas Expl. And ProductionMining

    Petroleum Refining

    $0.9$1.4

    $3.7$0.1

    Report No. FHWA-RD-01-156Corrosion Cost and Preventive Strategies in the United States, Gerhardus H. Koch, M.P.H. Brongers, N.G. Thompson, Y.P. Virmani, J.H. Payer, Office of Infrastructure Research and Development Federal Chem., Petrochem., Parm.

    Pulp and PaperAgricultural

    Food Processing

    $1.7$6.0

    $1.1$2.1

    Payer, Office of Infrastructure Research and Development Federal Highway Administration, Department of Transportation, 2003

    Food ProcessingElectronics

    Home AppliancesDefense

    N l W t St

    $2.1-

    $1.5$20.0

    $0 1Nuclear Waste Storage $0.1

    Cost of Corrosion Per Analyzed Economic Sector, ($ x billion) $10 $20 $30$0 $40

  • Internal Corrosion

    External Corrosion

    Third Party Damage

    ASME Causes of Gas Transmission Incidents

    Unknown

    Incorrect Operation

    Misc

    Natural Forces

    Internal Corrosion

    Prev. Damgd Pipe

    Mfr

    Constr/Instal

    Other Failures Non-PipePipe

    0.0 5.0 10.0 15.0

    Vandalism

    Stress Corrosion Cracking

    Malfunction

    5% hot tap error

    6%other

    50% external interference15% corrosion

    7% ground movements

    17% construction andmaterial defects

    Source: EGIG-02, data period 1970-2001

    (stray current corrosion)

    C iAC-induced corrosion Crevice corrosion Corrosionunder disbonded coating

  • Bellingham, WA

    Carlsbad, NM

    Edison, NJ

    5

    Gas explosion caused by charged soil (15 m x 34 m) due to corrosion

  • 2.

    pH

    A W P b d P b d C t l f Pi li C i 2nd d

    7

    A. W. Peabody, Peabodys Control of Pipeline Corrosion, 2nd .ed.

    CP

    2.

    40 10-2

    10-1

    /y 10-710-6

    10-5

    10-4

    10-3

    i, A

    /cm

    2

    30

    ate,

    mm

    /

    10-8

    10 7

    -2.0 -1.5 -1.0 -0.5 0.0 0.5 1.0 1.5

    E, V/CSE

    20

    rosi

    on R

    a

    10

    mu

    m C

    orr

    0Max

    im

    -800 -600 -400 -200 0 200

    Potential, mV/CSE, /

  • 5835 2

    100

    35.234.23125.4

    10

    11

    0 1

    0.04

    0.1

    0.0180.01

    1000 800 600 400 200 0 200-1000 -800 -600 -400 -200 0 200

    (mV/CSE)

  • : , : Sta.No. 621+00

    (A) (B) (C)

    D1 : 300[mm] PE 3[m] 3 - [A] ( : 2.5m) D2- , [B] ( : 5m) - [C] ( : 4.5m, B )

    D3

    D4

    D5

    D6

    (mm)

    (mm)

    (mm/y)

    (mm/y)

    (A) 1.75 3.0 0.48 0.82

    (B) 1.74 3.8 0.47 1.04(B) 0 0 0 0

    3.

    500 33 000

    ()

    500 33,000 200

    700 33,000

    - (, ) : 40- : 10km- : 2km : 2km - : 20- 1 : 50( 1, Deep well 3)

    - : 50 x 5 x 2(40) = 500 , : 5/ x 40 = 200- 700

    * (1 2 : 1 3 4 ) (1., 2, : 1, 3. , 4. )

    10km - 3.3/m x 10,000m = 33,000 47 . 47 .

  • 1)

    1) : 1)

    2) 1) :

    2) :

    3)

    4)

    5.

    - , , - - - : cathodic protection (/)

    - -

    - () :

  • 5 5.

    -

    :

    - : ,

    -

    : ( 850mV)

    : (-850mV)

    - : , (CIPS,DCVG) /

    - DCVGCIPS

    Immediate

    ScheduledMonitored

  • 5.

    (ECDA) (ECDA)

    (CP) ,

    SOIL CORROSIVITY

    5.

    (Gas Transmission IM Rule), 49CFR192.923-931 (2003) 10 HCA 5

    7

    (ECDA) (pressure testing) , e.g., In-line inspection (MFL-ILI)

    / (2003) 1MPa / / 15 1MPa / / 15

    5 ASME B31.8S NACE RP0502 (Methodology for ECDA)

    Shall/Must Should Statements

  • T/B

    ECDA

    3, 4

    ( ) Pin-Hole

    ( ) - - microbiologically influenced corrosion; MIC

    -

    ( )

    - (-)- : 3,2037,536cm- (SO4-2) (432.74/)

    - .- - ()

    (pitting) - SRB

    - , (air penetration)

    - ..- -

    - ..- .

    -

    (ECDA)

  • PRE-ASSESSMENT

    Risk Assessment

    INDIRECT EXAM. DIRECT EXAM.

    POST ASSESSMENT (region)

    IMMEDIATE

    POST ASSESSMENT

    (CIPS/DCVG/)

    IMMEDIATESCHEDULEDMONITORING

    CIPS/DCVG/

    SEVERE

    MODERATEMINOR

    0

    1324+0 1326+0 1339+0 1372+0

    400

    -200

    -600

    -400

    (m

    V)

    -800

    850mV

    -1200

    -1000-850mV

    -1200

    2000 2001 2002 2003 2004 2005 2006 2007 2008 2008

    : . ( )(/? ? 3 ?)

  • 3 (DC G) (DCVG)

    (CIPS) () ()

    (, ) (, )

    (anodic interference)

    ,

    (cathodic interference) ( )

    /

    (combined interference)

    : Control of Pipeline Corrosion, A.W. Peabody

  • (mV) - 100 VDE-0150 20 BS 7361, part 1

    [ON - OFF]>0

    [ON OFF]

  • 100200

    -300-200-100

    0100

    -700-600-500-400

    -800

    030

    563

    091

    712

    1018

    0021

    1221

    2021

    25.5

    2140

    2160

    2180

    2200

    2220

    2240

    2280

    2300

    2350

    2360

    2402

    2407

    .224

    2024

    4024

    6024

    8025

    0025

    2025

    4025

    6025

    8026

    0026

    2026

    4026

    6026

    61.7

    2680

    2700

    2708

    .730

    00

    (m) (m)

    On/OffOff Off

    ON/OFF 0

    (+)

    On

    On

    ( ) !!!

    On

    Off

    On

    Off

    !!!

    DCVG (pulsed-direct current voltage gradient) method

    2 3 1520

    2~3m -5

    0

    5

    10

    Defectial D

    iffer

    ence

    (m

    V)

    0 1 2 3 4 5 6 7 8 9

    -25

    -20

    -15

    -10Defect

    Pote

    nti

    Measure Point

  • 30

    40

    10

    20

    mV)

    20

    -10

    0

    (

    -40

    -30

    -20

    -400 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500 1600 1700 1800 1900 2000 2100 2200 2300

    Dstance (m)

    (TB)

    32 /2,400m: 75m 1

    (TB) 4 4 32 23 41 104

    - (2-3m )- - -

  • -500

    -700

    -600

    -900

    -800CP criteria

    TB 3VC

    SE)

    1100

    -1000

    900

    TB 1TB 414 7mA

    TB 511.4mA

    TB 315.4mA

    TB 80 mA

    TB 9ent

    ial (

    mV

    -1200

    -1100 TB 126.8mA

    TB 2

    14.7mA

    TB 619.2mA

    TB 734.3mA

    TB 925.2mA

    P/S

    pot

    e

    -1400

    -1300 55mA

    0 1 2 3 4 5 6 7 8 9 10-1500

    Distance (km)Distance (km)

    CIPS !!!Test points TP TP

    0

    (OFF) (ON) Defect 1

    (43V, 7A) (43.3V, 17.7A)

    -1000

    -500

    0

    -850mV

    -2000

    -1500

    mV)

    : -728mV

    -3500

    -3000

    -2500

    CSE(m

    -4500

    -4000

    -5000 0 100

    200

    300

    400

    500

    600

    700

    800

    900

    1000

    1100

    1200

    1300

    1400

    1500

    1600

    1700

    1800

    1900

    2000

    2100

    2200

    2300

    2400

    Distances(m)

    2006 ( , ): , : ,

  • (< 3000 5 000 ohm cm) (< 3000 ~5,000 ohm.cm)

    Wenners four electrode method (ASTM G57)

    (cm) Defect 1

    1.E+05(43V, 7A) (43.3V, 17.7A)

    1.E+04

    cm)

    (

    c

    5,000(cm)

    1.E+03 0 1 0 20 30 40 50 60 70 80 90 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24

    00 00 00 00 00 00 00 00 00 000 100 200 300 400 500 600 700 800 900 000 100 200 300 400

    Distances(m)

  • (urgency of excavation) (Immediate action required): I II (Immediate action required): I, II (Scheduled action required): III, IV

    (S it bl f it i ) V VI (Suitable for monitoring): V, VI

    (minor) (moderate) (severe) > 10,000 cm 5,000 10,000 cm < 5,000 cm

    CIPS 0 85V 0 85V 0 75V 0 75VCIPS < -0.85V -0.85V < < -0.75V > -0.75V

    CIPS I II

    III

    IV IV

    V VI

  • VI 7 7 13 3 2 0 32

    / 6 6 12 11 6 0 41(TB) 1 0 3 0 0 0 4 1 1 2 0 0 0 4 2 6 5 4 6 0 23

    1: D 63

    V CSE

    (mV)

    CIPS

    CIPS

    PCM2.5

    2.0

    dBmA

  • 1)

    2)

    pH 3) )

    : 80cm

  • 2.8mm2.8mm

    3.1mm

    2.1mm 1.5mm

    10% (HCl)

    (FeSx) H2S SRB

    2)x(0xCl2FeSxHHCl2FeS 2 2)x(0xCl2FeSxHHCl2FeS 22x

  • 3000

    O

    1000

    2000

    S

    Si

    3000 0 1 2 30

    FeCaAl

    2000

    3000

    O

    1000Ca

    Fe

    Si

    0 1 2 30 S

    keV

    Si

    S (SRB )

    8

    109109

    8

    109

    106

    107

    108

    oil)106

    107

    108

    soil) 106

    107

    108

    soil)

    103

    104

    105

    SRB

    (cel

    ls/g

    -s

    3

    104

    105

    SRB

    (cel

    ls/g

    of

    103

    104

    105

    SRB

    (cel

    ls/g

    -s

    0 10 20 30 40 50 60100

    101

    102

    102 103 104 105 106101

    102

    103S

    -0.2 0.0 0.2 0.4 0.6 0.8100

    101

    102

    0 10 20 30 40 50 60

    Clay Content (%)10 10 10 10 10

    ( cm)

    108

    109Eh (V/NHE)

    108

    109

    106

    107

    s/g-

    soil)

    105

    106

    107

    s/g-

    soil)

    ,

    104

    105

    APB

    (cel

    ls

    102

    103

    104

    SRB

    (cel

    ls

    102

    103

    102 103 104 105 106 107 108 109

    SRB (cells/g-soil)

    0 10 20 30 40 50100

    101

    Water Content (%)

    APB

  • ~~~~*~

    .

    SRB () K Kasahara et al () K. Kasahara, et al.,

    Corrosion, 55(1) (1999) 74

    OH2He2OH2 22

    .

    22

    .

    : 950mV: -950mVCSE

    46

  • pH (~10)

    pH 1) pH (

    , OH- pH

    OH2He2OH2 22 1) pH ()

    2) pH pH

    pH pH>10~11 pH>10 11

    ,

    . pH< 8

    (ECDA) ( ) )

    SRB

    ? ? .

  • / /

    1)

    1) : 1/TB1 1) 2) 3) ( )

    1) : 1/TB1 ,

    2) . ,

    3) 4) 4)

    A. 1) 2)

    3) 4)

    B. ECDA

    5)

    B. ECDA

    ,

    ,

    .

    2009.10.05. ~ 2010.08.30. (330)

  • ,

    (11.33km)

    (25.12km)

    R t th

    (25.12km)

    (2.24km) Remote earth

    NO /10 11 12 1 2 3 4 5 6

    (%)1 2 3 4 1 2 3 4 1 2 3 4 1 2 3 4 1 2 3 4 1 2 3 4 1 2 3 4 1 2 3 4 1 2 3 4

    1001 100 902 100 203

    100 0

    4 100 0

    5 100 0

    6 () 100 0 0

    7 100 0

    8 (remote earth bed) 100

    8 09

    100 0

    10 10010 0

  • / . (, ) ( )

    () +()

    -300

    0

    () +()(STA 29+37.91)

    STA 73 80V 9A

    -

    -600

    , mV

    ,

    - : ~0.2A ( 9A 2 2%)

    -1200

    -900

    E,( 9A 2.2%) : 11 ( 2A ,

    2A/12A = 17% )-1500

    -15 -10 -5 0 5 10 15Distance, m

  • (, , )

    : : : 9A 3A () (~33%)

    1) Metallic contactblacktop

    blacktop 2) Electrolytic contact

    - () ( , spacer )

  • ( )

    TB5

    -

    l (m

    V)

    TB6TB4

    Pote

    ntia

    Time (day)

    TB TB

    blacktop

    (3p) (2p) (3p) (2p)

    Referenceelectrode

    1) / TB 2)

    - ( ) ( ) 3) (e.g., mortar)

  • : 11 1

    : 30m

    (, , , )

    ()

    ( 11) 8.1A (0.2x11 = 2.2A ) 2.5km: 800mm

    PE 30m 7.1A (2.2A )

    PE 8.4A (2.5A ) 12.8A 5.9A

    - - , 120% (5.9A 12.8A)

    GPSGIS

    Satellite Communication

    Wire or WirelessNetworks

    (GSM, CDMA, RF, Zigbee, etc)

    Communication

    Rectifier RectifierTB 1 TB 2

    Remote Monitoring

    Remote ControlRectifier

    Remote Monitoring

    Remote ControlRectifier

    ReferenceElectrode

    ReferenceElectrode

    Data Logger Data Logger

    Anode AnodeCP current

  • () () 5,578 1,611 15,000 67

    ON

    OFF

    ON

  • 0.0

    0.2

    0.4

    SE

    0.6

    entia

    l,V CS

    0.8Pote

    (off): 06-08 15:00 ON: 6-26 18:30

    1.0START: 06-07 19:00

    1.20 24 48 72 96 120 144 168 192 216 240 264 288 312 336 360 384 408 432 456 480

    TIME,h

    0.0

    0.20.1

    0.40.3

    0.60.5

    tial,V CS

    E TB1

    TB2

    TB3

    0.80.7Pot

    ent

    TB4

    TB5

    TB6

    1 00.90.8

    TB7

    TB8

    TB9 OFF

    1 21.11.0

    START ON

    1.20 24 48 72 96 120 144 168 192 216 240 264 288 312 336 360 384 408 432 456 480

    Time,h

  • P/S IR free CP criteriaP/S IR-free CP criteria

    TB5

    tial (m

    V)

    TB6TB4

    Poten

    t

    TB4

    Time (day)

  • 19181717161514

    13

    +5V

    1312

    1110

    1+5V1098

    7

    3

    2

    4

    5

    76

    510

    89

    64

    7

    4

    3

    1113

    1415

    16

    12

    -5V3

    2

    1

    1417

    1618

    19

    T1-17

    -1

    0

    1

    2

    l, V C

    SE

    -0.83V

    T1 15

    T1-18T/B

    T1 18 1 6-5

    -4

    -3

    -2

    Pote

    ntia

    -4.93V

    T1-15 T1-18-1 -6 0 20 40 60 80 100 120 140 160 180Time, s

    T1-11

    T/B

    T1 10

    T1-12

    T1-13 T1-10

    T1-14

    T1-16

    (EPR)T ()

    ()T/BT/B

    -1

    -2

    Pote

    ntia

    l, V C

    SE

    -2.66V

    -4

    -3

    0 20 40 60 80 100 120 140 160 180Time, s

    -3.00V

  • () / 3 000km 200km 3,000km 200km 100, TB 125

    () 3,000km 400km 50, TB 406

    BP ~ 5km (Rectifier 2, Data logger 10)

    () - 20 TB 8 20, TB 8

    Gas transmission pipelinesMunicipal water pipelines Gas distribution pipeline (Mokpo)Samsung BP Chemical

    2010 30, TB 40 Planned (2010)

    g

    5 5.

    / (ECDA ) / /

  • 4 CIPS

    POOR

    (ECDA )(5~10)

    ? YES

    DCVG

    : -850 mVCSECIPS:

    or NO

    or