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Application of ECDA
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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