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Safety and pipe integrity : from natural gas to CO 2 transport by pipe EGATEC 2011 Conference, May 12-13 th , 2011 Frederique Bravin GDF SUEZ DRI/CRIGEN

Safety and pipe integrity : from natural gas to CO2 … and pipe integrity : from natural gas to CO 2 transport by pipe EGATEC 2011 Conference, May 12-13th, 2011 Frederique Bravin

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Safety and pipe integrity : from natural gas to CO2 transport by pipe

EGATEC 2011 Conference, May 12-13th, 2011 Frederique Bravin GDF SUEZ DRI/CRIGEN

Outline

Worldwide CO2 transport characteristics

CCS within GDF SUEZ

CO2 transport: a link between capture and storage

Example of modelings

2 May 12th, 2011

CO2 pipeline transport is already

established (since the early 1970’s)

More than 6000 km CO2 pipeline worldwide (mainly in the US)

Total capacity : more than 50 Mt CO2/y

Is large volume CO2 transport already a reality ?

Transport by ship is also considered (LPG tanker conditions)

“CO2 terminals” already under exploitation (for inst. in Montoir de Bretagne)

CO2 tanker « Yara Gas II » - ©Photo: Per Kristian Rognes

3 May 12th, 2011

Is CO2 transport far different from natural gas transport expertise ?

Similar in many respects in design and operation to NG pipelines

BUT… significant differences

Higher pressure range (more than 80 bar)

Pumps rather than compressors

Thicker-walled pipes

CO2 is heavier than methane

Handling CO2 with different quality from different sources

©Photo : Médiathèque GDF SUEZ

4 May 12th, 2011

Mc Kinsey&Company, « CCS, Assessing the economics », Sept 2008

A possible deployment of the CO2 network ?

Geographical distribution of emitters and storage availability may have a strong impact on CO2 network deployment :

Regional availability of storage :

• Local/regional clusters

• Transnational networks

Emerging hubs :

• Starting from large CCS demo projects

• Located near large CO2 clusters and storage sites

5 May 12th, 2011

CASTOR, CESAR, DECARBit, ACCACIA, cryogenic

capture

CATO2, BIGCCS Pilot Nijmegen in

partnership with Hitachi and E.ON

Long term testing at Esjberg

Large demonstration Road.

250 MW post combustion in

Rotterdam

TRANSCO2

CATO2, BIGCCS, CITEPH

SaR-CO2, COSHER Pilot France Nord

Large demonstration Road.

5 km onshore + 20 km offshore

Pilot K12B since 2004 (injection & storage in

offshore depleted gas field)

MOVECBM, GESTCO, RECOPOL, Geocarbone…

CATO2, BIGCCS

Pilot France Nord injection & storage in deep saline aquifer

Pilot in depleted gas field (Altmark)

Industrial project partner in Snøhvit

Large demonstration Road.

considered depleted gas field operated by TAQA

Industrial project: Touat. Deep saline

aquifer

2000 2010 2015

Mostly through partnerships

Capture

Transport

Storage

2020 2030

R&D projects from CO2 capture to CO2 storage within GDF SUEZ CCS Corporate Program

6 May 12th, 2011

1 - SaR-CO2 “Requirements for Safe and Reliable CO2 transport pipeline”

Run as a JIP between : • Energy, O&G companies : E.ON, GDF SUEZ, ENI (CSM)

• Gas transporter : National Grid

• Pipe manufacturers : EUROPIPE, Salzgitter Mannesmann Linpepipe & Vallourec & Mannesmann Tubes).

Technical topics of SaR-CO2 organized in two separate Joint Industry Projects:

• SaR-CO2 – phase A (Led by SZMF) • Specification of operating and test conditions – pipe supply • Corrosion and stress corrosion control • Safety and reliability analysis • Analysis and publication •

• Follow up: • Specification of operating and test conditions – pipe supply • Fracture and fracture arrest • Analysis and publication

Status : ongoing – Schedule – phase A : Sept 2010 / March 2012

Three main investigation topics : • Likely composition and transport condition

• Requirement for corrosion and stress corrosion cracking resistance of steel pipes (including experimental tests)

• Improvement of existing safety and reliability know-how and experimental release data with small scale experiments

7 May 12th, 2011

Planning:

• After the first phase of the project (2 years), the partners expect to be able to recommend a site for the pilot facility.

Partnership:

• Industry : GDF SUEZ, TOTAL, AIR LIQUIDE, EDF, LAFARGE, VALLOUREC. • R&D centers : BRGM, IFPEN, INERIS, EIFER, GFZ.

Total budget:

• 54 M€ with 40% financed by ADEME’s research demonstrator fund.

2 - France NORD (FR) – PILOT Storage in deep saline aquifers

Main objectives:

• The project will examine the feasibility of installalling in a sedimentary basin in the north central part of France, a CO2 transport & injection pilot.

• Detailed technical studies will be conducted in order to select a suitable geological site for storing CO2.

Submitted and selected by to ADEME’s research demonstrator fund put in place after the French Grenelle Environmental Forum.

8 May 12th, 2011

3 - COSHER

Main characteristics: Objective: To support the development of safety models for high pressure CO2

transmission pipelines by gathering data from large scale CO2 release experiments

Approach: To carry out measurements to develop a generic understanding of the processes in and outside the pipeline in case of CO2 releases under different circumstances

A broad consortium of stakeholders including GDF SUEZ

COSHER aims to be complementary to other CO2 safety projects with which COSHER would like to collaborate on the basis of win-win

The detailed definition of the experimental and measurement programmes will be completed in June 2011. The next phase concerns the actual execution of the experiments.

Organisations potentially interested in participation are kindly invited to contact the project coordinator ([email protected])

9 May 12th, 2011

Transport : from capture to storage

Provide a framework accounting for current information about system constraints in the CCS

chain. Public sources. Constraints: need to generate usable knowledge in a relatively short time-frame, due to

several pilot facilities under design and / or construction in Europe. The system dimensions considered are :

• CO2 capture processes: post-combustion, pre-combustion, oxy fuel • CO2 pipelines transportation • CO2 storage in aquifers or depleted oil / gas fields.

Different issues on CO2 transportation:

• Internal corrosion control due to the transported fluid, i.e. CO2 + impurities left over by the different capture and post capture process

• Material behavior at low temperatures as reached during CO2 leaks on network components: is there a risk of embrittlement, and what material specifications are needed to avoid this?

• Health and safety issues related with dispersion tests and modeling for small leaks on network components.

10 May 12th, 2011

11 May 12th, 2011

Transport : from capture to storage

Capture

Transport

Storage

Composition

P, T

Corrosion

Health & Safety

Materials

CO2 compositions after capture processes on flue gas

12 May 12th, 2011

Transport operating conditions

Capture, transport and storage set composition constraints; storage and pipe length set pressure and temperature operating conditions.

13 May 12th, 2011

OLGA® : a powerfull simulation tool

OLGA 6.1 first commercially available transient simulator for CO2 transport

Applications examples : • determine pipe dimensions (steady state) • investigate flows instabilities in the pipeline and the risk of entering the two-phase region (transient) • procedures for start-up, shut-down and blow down of the pipeline which might lead to very low

temperatures and formation of solid CO2 (transient) • rupture scenarios : estimating emissions and monitoring pressures and temperatures (transient)

Model validation : • SPT group tested the functionality within the framework of a pilot

study • CO2 transportation from Kårstø/Mongstad to the Utsira/Johansen

formations • DNV and Gassco were clients of this study

OLGA provided results in accordance to the client expectations :

• CRIGEN inquired the single component addition module

14 May 12th, 2011

OLGA application

Experimental device, several goals : • leak diameter impact • P,T influence

OLGA simulations for flow conditions description :

• fluid properties fully described along the line • transient description of the leakage mass flow

evolution, depressurisation path and gas cooling • phase transitions taken into account

OLGA results used as input data for dispersion models :

• accurate description of the flow behavior inside the pipeline

• can complete monitored data and allows extrapolation for non investigated conditions

0

0,5

1

1,5

2

2,5

3

-5 0 5 10 15 20 25 30 35 40M

ass f

low

rate

[kg/

s]

Time [min]

liquid mass flow upstream of leakage

gas mass flow upstream of leakage

15 May 12th, 2011

Conclusion

16

CO2 transport is similar in many respects in design and operation to NG pipelines …

… but CO2 is a gas with its own specificities…

… this is why experimental data are needed...

… for updating modeling tools (usually used for NG) …

… so that safety and integrity of inhabitants and pipes are guaranteed.

May 12th, 2011