Advanced CO2 consequence modelling for safe CCS Agenda 2 01 Introduction 02 CO2 releases to the atmosphere 03 CO2 releases under water 04 DNV’s expertise in CCS DNV © Introduction 3 DNV © CCS: Carbon capture and storage in brief • CCS: important carbon abatement technology • Capture: millions of tonnes of CO2 from significant emitters • Transport: pipelines or ships before being injected • Storage: deep into the earth’s rock formations Source: Econnect Energy 4 DNV © Operational and planned capture capacity [Mt of CO2 per year] Properties of carbon dioxide (CO2) • Colourless, odourless & invisible gas at standard conditions Pure CO2 Phase Diagram • “Dense phase”: means liquid or supercritical CO2 Triple point (5.18 bara, -56.6°C) • Supercritical: viscosity similar to gas, density closer to a liquid • Dissolves in water to form carbonic acid 5 DNV © ation Satur Line Critical point (73.8 bara, 31.1°C) Gas phase • Only gas or solid phase at atmospheric pressure • Solid CO2: known as “dry ice” (-78°C) Liquid phase Solid phase Melting Line • Four phases: gas, liquid, solid and supercritical Pressure (bar) • Heavier than air; not reactive or flammable ion ine L at m bli Su Supercritical phase Atmospheric Pressure Sublimation temperature at atmospheric pressure: -78.5°C Temperature (°C) CO2 hazards • Asphyxiant when displacing oxygen in air • Impacts depend on location specific factors • Threat to life at concentration of 15% due toxicological impact • Animals may suffer hypercapnia and asphyxiation • Immediately Dangerous Life or Health (IDLH) of 4% • Dissolves to form carbonic acid • Absorbed in soil can cause vegetation die-off • Rapid expansion and phase change creates high velocity, low temperature 2-phase jet • Personnel exposed to cold jet of gas with entrained solid particles • Brief exposure harms delicate tissues • Prolonged exposure: cold burn and frostbite • Inhalation causes severe lung damage 6 DNV © CO2 HAZARDS • Reduced visibility within CO2 water vapour cloud • Stopping of internal combustion engine • Projectiles upon containment failure Hazard analysis software for safe CCS Phast Control CO2 hazards by modelling discharge, dispersion and toxic effects KFX Advanced CO2 discharge and dispersion modelling using computational fluid dynamics Image provided by the Global CCS Institute 7 DNV © CO2 releases to the atmosphere Source term and dispersion modelling 8 DNV © Dispersion of CO2 in the atmosphere 9 DNV © 100 mm pure CO2 release – video Dispersion of CO2 in the atmosphere 10 DNV © 100 mm pure CO2 release – video Phast™ consequence modelling CO2 releases to the atmosphere 11 DNV © Phast™ modelling LOC scenario Discharge Weather Toxic Dispersion Radiation Explosion 12 DNV © Phast capabilities for modelling CO2 • Release scenarios – source term: • Pressure vessels: leaks, catastrophic ruptures • Long pipelines (buried or above ground): punctures, full-bore ruptures • Dispersion: unified dispersion model (UDM) • Toxic effects: concentrations, probit, lethality levels 13 DNV © Phast extensions for solid phase CO2 • Phast generally handles fluids, not solids No solid CO2 modelling Solid CO2 modelled • Phast solid extensions for CO2 more than 15 years ago • Discharge: Solid effects accounted for in expansion from vessel orifice/pipe exit to atmospheric pressure Atmosphere • Dispersion: solid/vapour equilibrium, sublimation • No deposition of solid CO2 on the ground Vessel Pipe Vapour Liquid Flow Expansion zone https://www.sciencedirect.com/science/article/abs/pii/S0950423009001351 14 DNV © Vapour Liquid Solid Vapour Solid Validation of Phast for CO2 • Comparing Phast predictions with experiments is a crucial activity • DNV Spadeadam Research and Testing facility in Cumbria in the North of England • Numerous CO2 release experiments over the years • Phast validation: discharge and dispersion predictions compared against these experiments 15 Experiments Scenario Phase Hole size Year BP Orifice, horizontal Dense, Supercrit 6-26 mm 2006-7 Shell Orifice, horizontal Dense, Supercrit 6-25 mm 2010-11 CO2PIPETRANS Long pipe and orifice, horizontal Dense 10-150 mm 2012-13 COSHER Buried long pipe Dense 203 mm 2013 DNV © Phast CO2 pipeline releases • Phast pipeline release modelling • Fluid phases: liquids, vapour, super-critical • Accident scenario: full-bore rupture and partial breaches of a long pipe • Transient modelling • Accounts for valve action and finite pumped throughput • Subsea pipeline releases not modelled • Pipelines can be buried - crater effects Image provided by the Global CCS Institute 16 DNV © Phast buried CO2 pipeline releases • Phast models buried CO2 pipeline releases • Depth of soil cover and type of soil key inputs • Crater effects: dimensions, modified velocity and CO2 solid fraction • Stalling plume / gas blanket effect • Improved modelling released in Phast 8.9 June 2023 • Based on large-scale COSHER experiments 17 Crater from COSHER experiments International Journal of Greenhouse Gas Control 37 (2015) 340–353] DNV © Buried CO2 pipe releases: COSHER validation Maximum arcwise concentrations – observed vs predicted COSHER 1 (wind~4.7m/s) 18 DNV © COSHER 2 (wind~1.9m/s) 18 Do you recognize these photos? • Not a controlled experiment • COSHER large scale experiment was 8” • Accidental rupture of 24” CO2 pipeline near Satartia in 2020 • Leak size 9 times larger for the 24” Satartia rupture • Operator’s hazard assessment did not identify the scale of areas that could be affected https://www.phmsa.dot.gov/sites/phmsa.dot.gov/files/2022-05/Failure%20Investigation%20Report%20-%20Denbury%20Gulf%20Coast%20Pipeline.pdf 19 DNV © Significant improvements in upcoming Phast 9.1 • Liquid phase CO2 pipelines handled by Phast PIPEBREAK model • Extended Phast 9.1 model PIPEBREAK-II with crucial improvements for liquid CO2 pipelines • Initial rapid depressurization modelling for dense liquid • Modelling small holes (aperture ratio below 20%) • Modelling of liquid densities (inventories) Impact • More accurate liquid pipeline releases avoid workarounds • Avoid underprediction of fluid inventories 20 DNV © Phast PIPEBREAK-II: CO2PIPETRANS validation • DNV-led JIP, tests at DNV Spadeadam in 2012/13 • Full validation to be published, including dispersion • 200 m long pipe, 52 mm diam. P~100 bar, T ~3-14°C • Extended model validates well for CO2PIPETRANS • 8 releases from end of pipe, hole size: 10-50 mm • Test 6: hole size 10 mm, 3.6% relative aperture 21 DNV © Phast CO2 modelling: Further information Knowledge Centre: https://myworkspace.dnv.com/knowledge-centre/phast-and-safeti 22 DNV © Select publications on Phast CO2 modelling • Modelling of discharge and atmospheric dispersion for carbon dioxide releases (Journal of Loss Prevention, 2009) • Modelling of discharge and atmospheric dispersion for carbon dioxide releases including sensitivity analysis for wide range of scenarios (Energia Procedia, 2011) • Phast validation of discharge and atmospheric dispersion for pressurised carbon dioxide releases (Journal of Loss Prevention, 2014) • Verification and validation of Phast consequence models for accidental releases of toxic or flammable chemicals to the atmosphere (Journal of Loss Prevention, 2018) • Model improvements and validation for buried CO2 pipeline ruptures (Mary Kay O’Connor Safety & Risk Conference, October 2023) • A comprehensive pipeline source term model for pressurized/flashing liquids in Phast/Safeti (PIPEBREAK-II) (Global Congress on Process Safety, March 2024) 23 DNV © KAMELEON FIREEX KFX® dispersion modelling CO2 releases to the atmosphere 24 DNV © Atmospheric CO2 gas dispersion Typical release of liquid or supercritical CO2 25 DNV © CO2 dispersion in complex terrain • Full-scale CO2 dispersion predicted by KFX™-CO2 . • Multiphase CO2 dispersion from release of CO2 stored as liquid at 16 bar Release of 570t CO2 26 DNV © Predicted 4 vol % CO2 iso-surface development after rupture of a pipe connection below CO2 storage tank CO2 dispersion in complex terrain Reliable CO2 dispersion simulation technology, which accounts for effects of: • • • • CO2 thermodynamics Geometry Topography Atmospheric conditions, is a key to safe, full-scale CCS Major full-scale CO2 accident scenario simulated with KFX™-CO2 27 DNV © KFX™-CO2 Joint Industry Project (JIP) • Improve modelling and validation of complex thermodynamics processes for liquid releases including • Dry ice formation • Deposition of solid particles in complex geometries • Sublimation and dispersion of the resulting cloud • Account for 3D time varying effects of terrain, geometry and atmospheric conditions Provide a solid basis for improved CCS safety and for finding cost-effective technical solutions for design 28 DNV © CO2 concentrations predicted by KFX™-CO2 through a high-pressure CO2 release, including visualization of small, solid CO2 particles in the gas flow KFX validation for CO2 KFX vs. measurements BP tests 29 DNV © Shell tests KFX-CO2 JIP: Findings so far and next steps • Improved thermodynamic models predicting source characteristics at expanded conditions as input to multiphase dispersion • Improved models for gas dispersion being developed and tested focusing on: • Able to predict formation of solid particles, including sublimation • Improved treatment of wind boundary conditions and atmospheric turbulence for far-field dispersion including effects of water vapour condensation • 2-phase release of a mixture of vapour and solid modelled using interconnected Eulerian-Lagrangian model to describe behaviour of solid particles • 3D terrain and geometry modelling with automatic import of map data and CAD models for accurate dispersion simulation • Model for interaction of solid particles and surfaces will be implemented • Algorithms for automatic import and conversion of topography data into appropriate CFD geometry models • Testing against full scale scenarios being developed with customers • Investigation of effects of vegetation using 3D vegetation data 30 DNV © Effects of vegetation on CO2 dispersion • Vegetation has a huge capacity for storing and slowing down spreading of leaked gas because of: • high drag • low solid fraction • Leaked (dense) gas such as CO2 can be hold back in the forest making the lethal volume close to leak point much larger. 31 DNV © CO2 releases under water Source term and dispersion modelling 32 DNV © Under water CO2 release • Offshore CO2 pipelines might be a major hazard. • Pipeline failure CO2 plume under water CO2 cloud on the surface • Understand • behaviour of CO2 leaking from underwater highpressure pipelines • impact of CO2 releases on the safety of shipping or offshore infrastructure. • Input to QRA Setting up safety guidelines for CO2 offshore pipelines 33 DNV © Sea current Dissolved CO2 Coral reef Under water CO2 release – the questions to answer How is the plume of the release affected by a current above the release? How much of the gas is dissolved in the water at real, large-scale conditions? At what release rates/depth will bubbles start reaching the surface? What concentration of CO2 is recorded at the surface above the release? How is the dynamics of the bubble zone, and how can the interface be modelled in a best way? What are the safety distances on the surface for personnel for different subsea release rates? What is the extent of influence zones for marine life for different subsea releases? What are the capabilities to predict both the subsea and atmospheric CO2 plumes? Spadeadam Testing Centre - UK 34 DNV © Under water CO2 release – Experimental set-up DNV © Under water CO2 release 36 DNV © 4 mm upward CO2 release - video Under water CO2 release 37 DNV © 4mm downward CO2 release - video SINTEF SURE + DNV KFX™ for under water CO2 release modelling 38 DNV © DNV’s expertise in CCS 39 DNV © Developing the first international CCS standards DNV RESEARCH/JOINT INDUSTRY PROJECT • • • • • • • • CO2RISKMAN – Guidance on CCS CO2 Safety and Environment Major Accident Hazard Risk Management CO2 PIPETRANS – Guidance on transportation component of CCS projects CO2SafeArrest – Guidance on the efficient design of CO2 pipelines CO2QUALSTORE – Guidance for the selection and qualification of CO2 storage sites CO2 WELLS – Guidance on the risk management of existing wells at CO2 storage sites CO2 CAPTURE – Guidance on procedure for capture technology qualification HiPerCap – Development of novel Capture technologies ECO2 – Best environmental practice for offshore CO2 injection DNV RECOMMENDED PRACTICE DNV-RP-J201 Qualification procedures for carbon dioxide capture technology DNV-RP-F104 Design and operation of carbon dioxide pipelines DNV-RP-J203 Geological storage of carbon dioxide INTERNATIONAL STANDARD ISO 27919-1 Carbon dioxide capture – Performance evaluation methods for post-combustion CO2 capture integrated with a power plant ISO 27913 Carbon dioxide capture, transportation and geological storage – Pipeline transportation system ISO 27914 Carbon dioxide capture, transportation and geological storage – Geological storage DNV-SE-0160 DNV-ST-F101 Technology qualification management and verification Submarine pipeline systems DNV-SE-0473: Certification of sites and projects for geological storage of CO2 DNV-SE-0617: Qualification management for geological storage of CO2 DNV FRAMEWORKS FOR ASSURANCE SERVICES 40 DNV © Helping scale CCS: 200+ projects in past 10 years 41 CAPTURE TRANSPORT STORAGE • Fossil power plants • Natural gas CO2 reduction • Other industrial processes • Pipelines • Ships • Depleted oil or gas reservoirs • Saline aquifers • Enhanced oil recovery (EOR) • • • • • • • • • • • • • • • • • • • Cost estimations Introduction of new technologies Technology review and benchmarking Up-scaling risk assessment HSE risk assessment Accidental release and dispersion Value of avoided CO2 DNV © Corrosion Material selection and structural design Flow assurance and operational issues Accidental release and dispersion Concept design for CO2 ships Requalification of infrastructure Verification of storage sites Permanence of storage Risk management Monitoring and verification Public concern Transfer of responsibility DNV’s ongoing activities • SUB-CO2 Phase 3 • Skylark • CO2SafePipe • KFX-CO2 42 DNV © Summary • R&D pivotal to understand underwater and atmospheric CO2 releases and dispersion and its associated risks • Consequence modelling tools: Phast and KFX developed to handle key physical phenomena such as: • Sublimation • Solid deposition • Craters • Time-varying releases • Topography • Vegetation • JIP between DNV and partners contribute to developing models for our tools and setting up guidelines for safe CCS 43 DNV © Image provided by the Global CCS Institute Thank you digital@dnv.com www.dnv.com 44 DNV ©