Role of Corrosion Field Joint System Selection Criteria in ... · PDF fileCoating System...
Transcript of Role of Corrosion Field Joint System Selection Criteria in ... · PDF fileCoating System...
February 2015
McDermott International, Inc.
© 2014 McDermott International, Inc. All rights reserved.
Role of Corrosion & Field Joint Coating System Selection Criteria in
Submarine Pipelines Integrity
Nawin Singh
What is Covered?
Pipeline System
Pipeline External Corrosion & Impact
External Corrosion Coating Systems
Corrosion Coating Selection Criteria
Field Joint Coating Systems and Alternatives
Way‐forward
Conclusion
Why Pipelines and what they offer?
Lower cost
More energy transportation capacity
Feed different segments of the energy consumption
Safer & environment friendly mode of transportation
Negligible loss of product in transit
Pipeline External Corrosion
When pipeline is either buried or submerged in water,corrosive environment constitute between metal surface andits environment. Corrosion is the damage of a substancewhich is usually a metal.
The rate of corrosion depends on various parametersincluding Pipeline Operating Temp. Surroundings e.g. water quality Soil quality & burial status Interference with other facility
Pipeline Incident Statistics
Ground Movement, 3.3
External Corrosion26%
Internal Corrosion, 5.3
Materials Fault, 8.3
Human Error, 2.5
Other Natural Hazards0.3
Accidental TP damage, 33.5
Stress Cracking, 1.1
Malicious TP damage, 5
Incidental TP damage, 7.2
Construction Fault, 7.5
Source: Ref. 3 [ERM from CONCAWE – 1971-2010]
Pipeline Integrity & Corrosion Impacts
Cost of corrosion is upto 3%[2] of GDP for USA
For Oil and Gas Pipeline alone, it is approx. $7billion[2] peryear for USA
Corrosion rated as 2nd most common threat for pipelineintegrity [10‐26%[4] ]
Coating cost is only 5‐6%[19] of project cost but play veryimportant role in integrity.
Pipeline Corrosion Coating Developments
Coal Tar & Asphalt Enamel
Powder Epoxy
Two layer System
Multilayer polyolefin
[Source: www.brederoshaw.com]
Coating Type and Market Share
[Source: Ref. 10]
0
20
40
60
80
100
North America South America Middle East Europe North Africa Asia
FBE PE/PP Other
Industry Standards for External Coating
AFNORAFNOR
NF A49 706 (FBE)
NF A49 710 (3LPE)
NF A49 711(3LPP)
AWWAAWWA
AWWA C203 (CTE )
AWWA C213 (FBE)
BSBS
BS 4164 (CTE)
BS 4147 (AE)
CSZCSZ
CSA Z245.20 (FBE)
CSA Z245.21 (Olefins)
DINDIN
DIN 30670 (3LPE)
DIN 30678 (3LPP)
ISOISO
ISO 21809‐1 (3LPE & PP)
ISO 21809‐2 (FBE)
ISO 21809‐6 (2L FBE)
ISO 21809‐4 (2LPE)
Coating Selection Criteria
External Corrosion coating
Economics
Adhesion
PerformanceEase of application
Environment
[Source: Ref. 15]
‐ Material‐ Application‐ Repair
‐ Cathodic Disbondment
‐ Holiday
‐ Mechanical Properties‐ Electrical Properties‐ Ageing/Design Life
‐ Application Rate‐ Compatibility with FJC‐ Easily repaired
‐ Past experience of End User‐ Local Regulation‐ Surroundings
Coating Selection Criteria [Ref. 6, 7, 13, 18]
Typical Properties Single Layer FBE 3LPE 3LPP
Service Condition Upto 80°C(110°C)
Upto 65°C (80°C) Upto 110°C (140°C)
Typical Thickness 350m ‐ 600m 2.2mm to 4.0mm
Impact Resistance[@23°C]
>1.5J/mm >7J/mm >10J/mm
Cathodic Disbonding[@approx. 23°c for 28days]
<8.5mm < 7mm < 5mm
Adhesion Strength[@23°C]
Rating 1 to 3 > 100N/cm > 250N/cm
Suitability for CWC application or HDD or similar
Suitable with additional layer
Suitable Suitable
Damaged during Handling Moderate Low Very Low
Cost [16] Comparatively lesser than PE
High Relatively Higher than PE
Coating Selection Criteria
0
5
10
15
20
25
FBE 3LPE 3LPPRank
ing considered
on 1 to 3 Scale (b
ased
on 3 as su
perio
r)
Current Generation Coating System
Ranking index ‐ Coating system
Normal Temp. Limit Max. Temp Limit Impact Resistance Adhesion
Disbondment Indentation Resistance Cost Performance
Field Joint Coating (FJC) System – Why?
Corrosion control
To supplement CP System
Mechanical protection
Design Codes specify e.g. DNV RP F102, ISO 21809‐3 FJC System Why?
Compatible FJC system
Fusion Bonded Epoxy (FBE) FBE 100% solid liquids, epoxy, epoxy‐urethane Heat‐shrink sleeves (HSS) Cold and hot‐applied tapes
Three layer polyethylene (3LPE) Three layer HSS Multilayer flame spray with PE
Three layer polypropylene (3LPP) Three layer HSS Multilayer flame spray with PP FBE, spray applied adhesive, co‐extruded PP
[Source: Ref. 1]
FJC System Selection
Technique
Compatibility
Pipelay geographical location
Environment
Complexity
Ease of repair
Cost
Field Joint Coating ‐ Possible Alternatives
Protective Network Coating System (PNC)
Solid Polyurethane
Other alternative for fast curing
Compensation with CP
Example:
[Source: Ref. 5]
System Injection Molded PP PNC
Pre‐heat Temperature 230°C 230°C
Cycle time on 24” joint 8‐10 minutes < 6 minutes
Operating Temp. rating ‐‐‐ 150°C
Level of applicator expertise High Low
Industry Compliance Yes Yes
Impact of Improvement in FJC System
[Source: Ref. 5, 16]
Pipeline Details 24” OD, 100KM long
Marine duration for one joint with conventional FJC 12 minutes (with 4 WS & 3 station for FJC)
Marine duration for one joint with alternative for FJC 8‐10 minutes (e.g. with 5 WS or PNC or other alternatives)
Saving per joint on marine duration 2.5 minutes
Total marine duration 341 Hrs / 14 Days
Saving on Marine Cost(assumed $400K/day)
5.6 MM $
Girth Weld Shrink Wraps $ 75 /meter2 [Ref. 16]
Total area (approx.) 4712 m2
Cost on account of FJC $ 354 K
Cost for additional anode $ 225 K (lesser than FJC material cost*)
Saving It seem approx. 5 MM$ on account of marineduration can be realized per 100KM considering other aspect including specialized crew for FJC application
Way forward
External Corrosion Coating and Pipeline Integrity
Coating Failure mechanism and challenges
Coating Specification
Field Joint Coating Selection
EPCI contractor engagement
Interaction needs to be encouraged amongst the designengineer, coating material manufacturer, coating applicator,installation contractor and the end user to provide aneconomical solution and to enhance long term performanceof external coating system for pipeline integrity.
Conclusion
This presentation can be seen as the start of further discussion forthe Specification authors, Standardization bodies and subseaindustry as a whole to review
‐ The coating selection process in view of upcoming challengesin terms of high temperature pipeline, long lasting coatingsystem, minimizing or eliminating the failure
‐ Requirement and compatibility for field joint coating system
‐ Incorporating the ongoing innovation & researches
Question
What next of 3LPP for pipelines operating more than 140deg C?
References
Sl No. References
1 [Online] / auth. A JPCL eBook ‐ Protecting and Maintaining Transmission Pipeline. ‐ Technology Publishing Company. ‐ January10, 2015. ‐ http://www.paintsquare.com/store/assets/JPCL_transpipe_ebook.pdf.
2 [Online] / auth. NACE International. ‐ Corrosion costs and preventive strategies in the United States. ‐ January 11, 2015. ‐http://www.nace.org/uploadedFiles/Publications/ccsupp.pdf.
3 [Online] / auth. Petitt Glenn // www.erm.com. ‐ January 10, 2015. ‐ http://www.erm.com/en/Analysis‐and‐Insight/Publications/ERM‐paper‐on‐cross‐country‐pipelines‐failure‐rates‐as‐presented‐at‐the‐IChemE‐Hazards‐XXIII‐Conference/.
4 8th EGIG ‐ report no. EGIG 11.R.0402 [Report] / auth. European Gas Pipeline Incident Data Group. ‐ Groningen : EGIG, 2011.
5 A New 3LPP Offshore Field Joint Coating [Conference] / auth. Mallozzi Meghan and Perez Mario // Corrosion Conference &Expo. ‐ USA : NACE International, 2010. ‐ Vol. Paper No. 10010.
6 External coatings for buried or submerged pipelines used in pipeline transportation systems ‐ Part 1: Polyolefin Coatings[Book] / auth. International Organization for Standardization. ‐ Switzerland : ISO, 2011. ‐ Vols. ISO 21809‐1.
7 External coatings for buried or submerged pipelines used in pipeline transportation systems ‐ Part 2: Fusion bonded epoxycoating [Book] / auth. International Organization for Standardization. ‐ Switzerland : ISO, 2007. ‐ Vols. ISO 21809‐2.
8 Fast Set Polyurethane Coatings ‐ High performance, cost effective alternatives for field joint coating [Report] / auth.Schertzer Richard. ‐ Canada : [s.n.].
9 International Experiences with Cathodic Protection of Offshore Pipelines and Flow lines [Report] / auth. TWI for PetroleumSafety Authority Norway. ‐ Norway : TWI Ltd., 2007.
References
Sl No. References
10 New Challenges and Developments in Pipeline Coatings [Article] / auth. Guan Shiwei William // North American Pipelines. ‐[s.l.] : www.napipelines.com. ‐ January/February 2010.
11 Offshore Pipeline Coating for Field Joints ‐ why? [Conference] / auth. Surkein Michael, Melot Denis and Eric Agel // Corrosion Conference & Expo. ‐ USA : NACE International, 2013. ‐ Vol. Paper no. 2258.
12 Performance of European cross‐country oil pipelines ‐ Statistical summary of reported spillages in 2012 and since 1971[Report] / auth. CONCAWE ‐ Conservation of clean air and water in Europe. ‐ Brussels : CONCAWE, 2013.
13 Plant‐applied external fusion bond epoxy coating for steel pipe [Book] / auth. CSA Group. ‐ Toronto : Canadian StandardsAssociation, 2010. ‐ Vol. CSA Standard Z2245.20.
14 Polypropylene Coatings for High Temperatures and Thermal Insulation of Pipelines [Conference] / auth. Turner Barry J. //Corrosion Conference & Expo. ‐ USA : Nace International, 2011. ‐ Vol. Paper no. 11030.
15 Review of Pipeline Coating Systems from an Operators Perspective [Conference] / auth. Thompson Ian and SaithalaJanardhan Rao // Corrosion Conference & Expo. ‐ USA : Nace International, 2013. ‐ Vol. Paper No. 2169.
16 Thick Film Coating Systems Technology Trends [Conference] / auth. Osborne Michael // PDA Annual Conference. ‐ Houston :PDA, 2014.
17 Trend in Pipe Coating Selection Process [Conference] / auth. Surkein Michael B. and LaFontaine John P. // InternationalOffshore and Polar Engineering Conference. ‐ Beijing : ISOPE, June 2010.
18 DIN German Standard for Polyethylene coatings on steel pipe and fittings – requirement and testing DIN 30670. ‐Germany : Deutsches Institute fur Nomung, 2012
19 www.bric.com [Online] / auth. Dasgupta Chanchal. ‐ January 12, 2015. ‐ http://www.bric.com/news/articles/new‐development‐in‐3lpe‐coating‐for‐pipeline‐protection.html.