cocate safety assessment pipeline export...
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COCATE Safety Assessment Pipeline Export SystemCOCATE WP 3: Safety Global Capture to Storage Transport Network
Menso Molag and Mark Spruijt
Menso Molag and Mark SpruijtCOCATE Safety Management
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Safety Assessment Pipeline Export System
Background WP3
Cocate WP3 Tasks, deliverables, partners
Release models high pressure CO2 pipelines
Dispersion released CO2
Vulnerability models
Further activitiesFurther activities
Menso Molag and Mark SpruijtCOCATE Safety Management
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QRA of CO2 pipeline Rotterdam - Amsterdam
Diameter: 0.65 mLength : 83 kmP 10 22 bPressure: 10 -22 bar
Menso Molag and Mark SpruijtCOCATE Safety Management
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Risk assessments CO2 pipeline
Failure cases: 20 mm hole and full bore rupture
Pipeline owner [2004] : 10-6 lethality distance 3.5 m from pipeline
Hoofddorp assessment [2005]: 1% lethality distance 200 m
TNO [2008] : lethality risk < 10-6 per year, 1% lethality distance 60 m
International comparison (Koornneef [2010]): 10-6 lethality distance : 0 – 200 mSafety distance : 0 – 7.2 kmSafety distance : 0 7.2 km
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Uncertainties QRA CO2 pipelinesKoornneef [2010]
Influence on risk
Failure scenario ++Failure scenario ++
Release frequency +
Vertical / horizontal Jet +++
Gas release or gas/solid release ++
Crater formation + loss of momentum ++
Meteorological conditions +Meteorological conditions +
Terrain altitude (obstacles, slopes/hills) ++
Human vulnerability model +++
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Cocate WP3: Objectives, tasks, partners
Objective: Define, quantify and analyse HSE risks of CO2 collecting network andtransport chain
Tasks:1. Development of safety management toolkit (DNV, IFP, TNO)p y g ( )2. Risk assessment collecting network (DNV)3. Risk assessment transport systems (TNO, DNV)4. Risk assessment integrated chains (TNO, DNV)
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TNO researchSmall scale release experimentspModelling of the 2 phase outflow and rain-out of solid CO2Dispersion of dense CO2Vulnerability of CO2
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CATO 2 programme:Small scale high pressure CO2 release experiments
TNO micro scale tests:• Release from 1 litre vessel• Nozzle opening : ¼ and ½ inch• Pressure : 60, 80, 100, 120, 150 180 bar
Objectives• Rapid study of phenomenap y p• Valve selection• Feasibility of Measuring techniques• IR (turbulence), high speed camera (particle size)
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CATO2 experiments: Kema Research/TNO
500 litre high pressure vesselNozzle length : 100 mmNozzle diameter : 1/8 inch, ¼ inch, ½ inchInitial CO2 pressure : 80 120 150 barInitial CO2 pressure : 80, 120, 150 bar
MeasurementsVessel : pressure, temperature, heat flux, liquid levelJet : CO2 concentration, T, velocity,
s/l/g mass fraction, air entrainment, condensation/freezing water
Menso Molag and Mark SpruijtCOCATE Safety Management
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Graag foto opstelling toevoegen
Menso Molag and Mark SpruijtCOCATE Safety Management
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Graag foto opstelling toevoegen
New solid CO2 formation model
Developed within TNO [1] as part of the Effects soft ware
Used within COCATE to get an idea of differences between severalUsed within COCATE to get an idea of differences between several codes/methods
CO2 solid formation
1. mechanical break up
2. flashing
3. evaporation and freezing
The result for CO2 is a solid particle diameter distribution
[1] “Assessment of particle size distribution in CO2 accidental releases” C E C Hulsbosch-Dam M P N[1] Assessment of particle size distribution in CO2 accidental releases , C.E.C. Hulsbosch Dam, M.P.N.
Spruijt, A. Necci, V. Cozzani, Journal of Loss Prevention in the Process Industries 25 (2011) 254-262
CFD:CO2 Dispersion of hypothetical worst case scenario pipeline rupture Le Havre -Rotterdam
Worst-case CO2 release scenario:
Massflow 1400 kg/s gaseous CO2“Zero”-momentum release (circularZero -momentum release (circular
release d=100m)Hilly terrain, distance to “village” 1 5km1.5km,
altitude difference 50mdomain dimension 2x2km
COCATE: Heavy gas continuous release in hilly terrain Wind 1.5m/s: Surface CO2 molar fractions
Massflow: 1400kg/s CO2
CO2 contours for weather conditions without wind and 1.5m/s windspeed:No wind: Up to 11% at lowest domain boundaries1.5m/s wind: 1% molar fractions at downwind domain boundaries
No wind: Surface CO2 molar fractionsNo wind: Surface CO2 molar fractions
release point)
Terrain topology (altitude)
Vertical distance [m] of 10 vol.% and 1 vol.% CO2 above ground level
10 vol %10 vol %
Maximum 10m at depressions Up to 5m at downwind
No wind Wind 1.5m/s
p ppositions
1 vol %
Terrain topology (altitude) Surface CO2 molar fractions
Up to 20m in front of local hills Up to 20m in front of local hillsat downwind positions
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Vulnerability of CO2 inhalation
TNO (inert gas), 2006 : Pr = -63.3 + ln (C5.2 . t) (C mg/m3, t min)
HSE (CO2) , RR749, 2009: Pr = -90.8 + 1.01 ln (C8 . t) (C ppm, t min)
E 1% letality 50% letalityExposure 1% letality[vol. % CO2]
50% letality[vol. % CO2]
[min] HSE TNO HSE TNO
1 11 18 15 28
10 8 11 11 1810 8 11 11 18
30 7 9 9 15
60 6 8 8 13
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Further activities
DNV: Bayesan Network Modelling + risk assessment framework
TNO finalize release modelling and consequence models
DNV: Risk assessment of collecting network + ship transport
TNO: risk assessment pipeline Le Havre – Rotterdam
DNV/TNO; Risk assessment CCS chain
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