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1
Proposal of Countermeasurefor Cargo Oil Tank Corrosion
by Anti-Corrosion Steel
JAPAN30th November 2006
MSC/82/23/8:Safety of Double-Hull Tankers
2
Contents
1. Values of anti-corrosion steels
2 Development of Anti-Corrosion Steels for COT/Bottom Plates (Actual Vessel Results)
3 Development of Anti-Corrosion Steels for COT/Upper Deck Plates
4 Conclusion~ Future Works ~
3
1-1 Corrosion Problem in COT of Crude Oil Tanker (Bottom and Upper Deck Plates)
Inner Bottom
Upper Deck
Inert Gas
H2S
Crude Oil
Sludge, Drain Water
Upper Deck⇒ General Corrosion
Bottom ⇒Pitting Corrosion
4
1-2 A New Countermeasure for COT Corrosion
Is ‘Coating’ the only answer to The Problem?
Constant quality and reliabilityLess Inspection and Less Maintenance during service Minimize the Environmental loadProtect Worker’s healthRecycling after scraped down …
・The Corrosion Test Method has been already established.・Anti-Corrosion Steels for COT has been also developed.・Large scale field test on actual vessels has been finished.
Anti-Corrosion Steels can provide sophisticated solution.Up to now …
The problem is not only corrosion, but also …
5
1-3 The Studies on COT Corrosion2000 2002 2004 20061998
Shift to Double Hull Tanker1990~
1999~2002 Panel SR242 committee(The Shipbuilding Research Association of Japan)
2002~
2003~Field Test on actual Vessels
Anti-corrosion steelsLaboratory Test
Scientific Research & understandingof the corrosion phenomena
(Over 10 VLCC s)Basis for Anti-corrosion SteelCorrosion test method
7
Contentsa) Mechanism of pitting corrosion on bottom platesb) Important Basis for Anti-corrosion steelc) On Board Evaluation results (Steel-A)d) Benefit of Applying Steel-Ae) Property of Steel-Af) Other developed Anti-corrosion Steels
(Steel-B,C)g) Summary
8
a).1 The facts of Pitting Environment Onborad (New Finding by SR242)
pH of PIT inside: low
(Lower than 1.5)pH about 1.5pH about 1.5
COT No Na T-Fe Fe3+ Cl- SO42- S2O3
2- pH H2SDH-1 13600 2 2 42500 14 ND 7.0 NDDH-3 1S 40000 42 11 48000 1470 ND 7.2DH-3 2P 40000 2.5 1 54000 1350 ND 7.5
Chemical analysis of water sampled from COT bottom (ppm) (crude oil loading Condition)
High concentration of NaCl solution was detected: NOT seawater
High Conc.of Cl-in water
(10mass% NaCl)
solid state S exists
Chemical analysis of sludge sampled in COT
I.D.Total Swt%
Total Fewt%
pH10g/100cc
Cl-
mg/kg
SO42-
mg/kgS2-
mg/kgSludge-A 2.3 19.7 4.5 83 151 4Sludge-B 7.5 22.8 6.8 766 2570 319
Solid Water solubles
9
a).2 Environment inside Pit
Target Environment
crude oil
BrineNot Sea Water
pH~0.85NaCl10%pH~0.85NaClNaCl 10%10%
Sulfur
Inert gas + H2S+O2
Brine (Cl- )Not Sea Water
Crude Oil
Oil coating(Crude oil + Sludge)
Defect
10
a).3 Simulated corrosion test based on the FACTS& the Newly Developed Steel
Beaker
Specimen
Test solutionNaCl 10%pH~0.85
0
0.2
0.4
0.6
0.8
1
1.2
Conventional Steel A
Ratio
of C
orro
sion
Rate
Steel-A
Conventional
Developed Steel-A provides excellent anti-corrosion Property
11
b).1 Pit Growth Stops at a dock
Pitting Stops
Pit D
epth→
Dock Ship Age→
New Pitting starts at new location
12
b).2 Mechanism of termination of Pit Growth at a Dock
Findings- Pit growth terminates at dock inspection- New pit appears at new location.
New Finding New Finding bySRbySR--242 Result242 Result
(1) Under servicing condition
(2) Dock inspection
(3) Re-Start of service
(4) Nuclear of new pit
Sludge & Corrosion products
Oil coating
Cleaned Steel Surface = No oil coat
Oil coating ,Sludge & Corrosion productsare cleaned and dried for inspection
Cleaned and dried pits are re-coated by new crude oil
New oil coat = Resetting insulating condition
defect
New defect in oil coat =Nucleation of pitting
New defect : by COW, Water …..
(1) Under servicing condition
(2) Dock inspection
(3) Re-Start of service
(4) Nuclear of new pit
Sludge & Corrosion products
Oil coating
Cleaned Steel Surface = No oil coat
Oil coating ,Sludge & Corrosion productsare cleaned and dried for inspection
Cleaned and dried pits are re-coated by new crude oil
New oil coat = Resetting insulating condition
defect
New defect in oil coat =Nucleation of pitting
New defect : by COW, Water …..
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c).1 Max. Pit Depth of Conventional Steels Onboard Repair is Essential! (by Welding a/o Painting)
SRSR--242 Result242 Result
Conventional
Maxim
um P
it Dep
that
Dock
(mm)
15
c).2 Applied area of Steel A in a VLCC#3 and #4 P,C,S COTs have been built without coating 2 years and 3 month after building2 years and 3 month after building
COW applied every voyage=Damages the protective oil coating↓
Severe condition for the corrosion
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c).3 Number of Pitting over 4mm Depth (Onboard result)
020406080
100120140160
Conventional Steel A
Aver
age P
it Cou
nts (O
ver 4
mm D
epth)
ZERO
No pits over 4mm depth
Developed Steel A: No need to repair
2.25yearsOnboard Test
Conventional Steel-AZERO
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7 7 7 20 4 270
200
400
600
800
1000
1200
1400
3P 3C 3S 4P 4C 4SCOT Position
Pits
Coun
t ove
r 2mm
Dep
th
c).4 Pitting Frequency of Steel-A OnboardOnly very few shallow pits (Over 2mm less than 4mm)
are observed!
No Pits over 4mm Depth
Pits
Coun
ts ov
er 2m
mDe
pth
COT Position
Conventional
Max. Pits Counts Over 4mm Depth
18
0
2
4
6
8
10
12
3P 3C 3S 4P 4C 4S
COT Position
Observed Max pit depth
mm/at 1st Dock
COT built by NS-GP1 without tar epxy painting
No need to repair
c).5 Max. Pit Depth of The Steel-A Only pits less than 4mm depth!
Maxim
um P
it Dep
th at
Dock
(m
m)
COT Position
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c).6 Appearance of typical pitConventional Steel and developed Steel-A
Pit on Steel-A(Small and Shallow)(Small and Shallow)
Pit on Conventional Steel(Large and Deep)
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b) Important Basis for Anti-corrosion steel for COT/bottom platesPit Growth Stops at a dock
Pit D
epth→
Dock
Conventional Steel
Anti-corrosion steel
Make Low
Ship Age→
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d) Benefit of Applying Steel-A
0
2
4
6
8
10
12
0 2.5 5 7.5 10 12.5 15Ship Age / years
Maxim
um P
it Dep
th / m
m
Pit less than 4mm
Pit Stops at Dock
Steel-A
No repair
Pits Over 4mmConventional Steel
Repair being Essentialat EVERY dock
Pit Stops at a dock New Finding by SR242
Pits Less than 4mm +
IACS Rule requires repair over 4mm depth pits
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e) Property of Steel-A
A typical chemical analysis (mass%)
With Least Micro-alloy ElementsSteel-A established high corrosion resistance
↓Same Physical Properties to Conventional Steel
C Si Mn P S Al Ti CeqNewly Developed 0.124 0.331
AH32 0.140 0.20 1.09 0.018 0.006 0.031 0.014 0.322IACS Standard ≦0.18 ≦0.5 0.9~1.6 ≦0.035 ≦0.035 ≧0.02 ≦0.02 ≦0.36
meets IACS Standard (including all ally elements)
23
Specimen303K
Water bath
NaCl solution Including Sulfur
*Assuming that specimen iscorrespond to pit inside.
f) .1 Other Anti-corrosion Steel for Bottom Plates
Steel-B provides excellent corrosion resistance property for very high concentration of sulfur.
0
0.2
0.4
0.6
0.8
1
1.2
Ratio
of C
orro
sion
Rate
Steel-B
Conventional
24
f).2 Other Anti-corrosion Steel for Bottom Plates
Temp. 40°CGas13%CO2-5%O2-0.01%SO2-0.2%H2S-bal.N2
Pitting corrosion and corrosion productsPitting corrosion and corrosion productswere reproduced by simulated test.were reproduced by simulated test.
gas outlet gas inlet
artificial sea water
specimenssludge
gas outlet gas inlet
artificial sea water
specimenssludge
pits
10mmAppearance of specimen after corrosion test
Corrosion rate after 2.5 years estimated fromsimulated test
00.20.40.60.8
11.2
Conventionalsteel
Ratio
of co
rrosio
n rate Bottom
1/51/5
SteelSteel--CC
Steel-C provides excellent corrosion resistance in simulated environment of cargo oil tank.
25
g) Summary on Anti-Corrosion Steelsfor Bottom Plates
• Anti-corrosion steels (Steel-A.B and C) showed good corrosion resistance in laboratory simulated tests.
• Newly developed anti-corrosion Steel-A has been adopted to a VLCC/COTs without coating for 2years and 3 months.
• There was NO PIT over 4mm depth on steel-A onboard.She docked out with NO repair.
• The Validity of Steel A was conformed onboard. Potential Ability for Repair-Free was recognized based on “pit stops at a dock” and “Pit Depth less than 4mm”..
• With Least Micro-alloy Elements, Steel-A established high corrosion resistance.
↓Same physical properties to conventional steels.With Good Workability, the VLCC has been constructed.
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3.1 Corrosion of Upper Deck Plates
Inner Bottom
Upper Deck
COT Gas
H2S
Crude Oil
Sludge, Drain Water
Inner Bottom⇒ Pitting Corrosion
Cyclic Temp. ChangeUpper Deck⇒ General Corrosion
Bottom Plate⇒ Pitting Corrosion
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3.2 Corrosion test Results of Steel-CWet & dry cycle (50℃ 25℃)Simulated COT gas (13%CO2-5%O2-0.01%SO2-bal.N2-H2S 0.2%)
NaCl solution
gas outlet gas inlet
specimens
00.20.40.60.8
11.2
Conventionalsteel
Ratio
of co
rrosio
n rate
Upper deck
Corrosion rate after 2.5 years estimated from simulated test
Results of simulated corrosion test
1/41/4
SteelSteel--CC
Steel-C provides excellent corrosion resistance in simulated environment of cargo oil tank.
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・Based on the facts found by the SR242 investigation,Simulated test methods is developed.
・Developed Anti-Corrosion Steel for Upper Deck plateimproves corrosion resistance largely.
3.3 Summary on Anti-Corrosion Steel-Cfor Upper Deck
30
4. Conclusion• Anti-corrosion steels are countermeasure against Oil
Tanker Corrosion.• Corrosion Tests for COT bottom and Upper deck plates
has been developed.• Validity of Anti-corrosion steels was confirmed based on
laboratory tests and actual vessel result.• Potential ability for repair free for whole ship life is
recognized.• Anti-corrosion steel provides sophisticated solution for the
Oil Tanker safety problem.
31
~ Future Works ~2007/02 DE50
Proposal of Anti-Corrosion Steel Performance StandardOutline of the StandardSimulated test procedure
(Inner bottom, Upper deck)
2008/02 DE51
Decision of detailsAcceptance criteriaVerification