ccs - liquid logistics shipping concept - anthony veder vopak
DESCRIPTION
Presentation by Anthony Veder Vopak at the Global CCS Institutes 2011 Member's Meeting in RotterdamTRANSCRIPT
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GCCSI StudyLiquid logistic Shipping Concept
Lessons learned to date
5/13/2011 1
Rotterdam May 11th, 2011
Michael Tetteroo & Cees van der Ben
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CINTRA logistic concept
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• Bulk making/breaking for off shore CO2 storage• Intermediate Storage• Combine and link pipeline systems and barging/shipping routes: 4 routes• Provide independent custody transfer metering (for ETS)• Network building block (at rivers and coast lines)
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Hub service: CO2 transfer barge/ship pipe
PIPE
BARGE/SHIP
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PIPE
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CO2 Transport and Storage systems
• Transport from the Emitters via pipelines or barges;
• Collecting CO2 in storage tanks at the CO2 Hub;
• Loading sea vessels for transport to depleted offshore gas fields.
Liquefaction at the Emitter’s siteor at the CO2 Hub
Connecting Hub
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• Locking the sea vessel to a floating turret or loading tower linked with the sub-sea system of the depleted gas field;
• Injecting the CO2 into the porous rocks (depleted gas or oil field or aquifers, at required temp’s and pressures ;
• As an alternative, mooring near a platform for discharging the CO2 into a depleted field via the platform utilities
• Ship is designed to carry both CO2 and LPG
Connecting Hubto offshore trunk line
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Hub Concept Organic Growth Model:Asset build up follows the volume build-up
Source 1 Source 2
1. Early scheme: single source flow too small to justify off shore pipe
Source 3 Source 4 Source n
3. Final mature scheme:
12 2
3
5/13/2011 5Sink 1 Sink 1
Sink 3: EORat oil field
Sink 2 Sink n
pipe
2. Intermediate scheme: two combined flows do allow for an off shore pipe => ship moves into alternative CO2 or LPG service
3. Final mature scheme:multiple sources & sinks, both depleted reservoirs and EOR at production wells
1
2
Ship now could become pipe
line for 2 sources
2
Potentially ship that
used to sail on sink 1
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GCCSI LLSC study: lessons learned to date
General• Start engineering at the sink• Minimize CO2 composition requirements• Combining multiple emitters in one network is technically feasible. • No metallurgical/corrosion issues found other than water: dry at the
sourceSHE• No items of concern encountered• Low vessel collision risk due to high LCO density
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• Low vessel collision risk due to high LCO2 density• On shore pipeline through busy areas: 40 barCompression• Up to 100 bar: bull gear compressor (bull gear), beyond: pump.• Moderate ambient temperatures: no power consumption difference
between compression or compression/liquefaction/pumping.Pipeline• In dense phase in order to minimize costs.
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GCCSI LLSC study: lessons learned to date
Liquefaction• Optimum CO2 liquefaction condition: -50 ˚C, 7 bara.• Combining parallel compression and liquefaction in one
machine feasible.Storage• Terminal minimum storage volume: 10,000 m3
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• Terminal minimum storage volume: 10,000 m3
• Min. costs/m3: > 2000 m3 shop fabricated spheres• Other considerations may call for horizontal bullets.Legislation
Biggest remaining uncertainties: • CO2 custody transfer: who, when and to whom• Monitoring requirements in the mean time
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2.5
3
3.5
Ship transport capacity [mmt/yr]
• Loading & discharge 2000 t/hr• Sailing speed 15 kts• Voyage related spare 1 day
GCCSI LLSC study: lessons learned to date
ship sizes
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10,000 cbm ship
30,000 cbm ship
Distance [nm]
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LLSC mission statement
400
450
• Depleted gas field NS • Stand alone operation• Stay above hydrate formation bottom hole temperature: 13 ˚C• Challenges: � all solvable
� Intermittent flow � Pressure over sink life time: 150 – 400 bar at well head
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0 2 4 6 8 10 12 14 16
Time line (years)
Sh
ip m
an
ifo
ld p
ressu
re (
bara
)
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Shipping
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• LPG/CO2 carrier• 30,000 m3
• Stand alone operation• Onboard conditioning• Key challenge: uptime
• Conventional • X - bow
Source Anthony Veder, X-Bow® IP of Ulstein Sea of Solutions
Source: AnthonyVeder – IP Anthony Veder
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Conventional hull
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LOA 210 m DP 2
B 33.6 m Sailing speed 17kts (lpg trade)
T 11 m Gradual power generation build
Source: AnthonyVeder – IP Anthony Veder
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CO2Conditioning
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Source: AnthonyVeder – IP Anthony Veder
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Rotterdam distance to sinks
Dutch sinks are all within the 400 km range.
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Barging/shipping• No CO2 venting/re-liquefaction in transit• Barge max. LOA 135 m → 150 m in the future• Max barge size Ruhrgebiet → R’dam: 7500 tonnes (Ruhrgebiet →
Karlsruhe: 6000 tonnes)• Required ship sizes: 10,000 - 30,000 m3
• Ship min. required off loading temperature: 0 ˚C• => sea water suffices as heat source for LCO2 “vaporization”
GCCSI LLSC study: lessons learned to date
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• => sea water suffices as heat source for LCO2 “vaporization”Ship off loading• HP pressure CO2 unmanned off loading: technically feasible at
acceptable uptimes in deep and shallow water.• Depleted reservoir’s existing wells require retubing• Ship → sink batch injection technically feasible, multiple wells likely
to be required flow wise.• Tubing: low temperature material of construction.
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GCCSI LLSC study: lessons learned to date
Costs: contract duration
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Pipeline system tariffs are hurt the most by short term contracts
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Source: IEA GHG, 2004
Transportation Costs: insight evolution
LNG CO2
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CO2 CO2
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Costs
• CO2 transportation is to be considered as a regular infra structural project: 20+ year contract durations
• CO2 liquefaction’s energy intensity is relatively low => cost break even distances are
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cost break even distances are1. for on shore pipe versus barge: 200 km (and not 1500 km)
2. for off shore pipe versus ship: 150 km (and not 750 km)
• Depending on flow and distance the transportation costs may vary from 20 to 120 €/ton (20 year contract)
• Combining multiple emitters in one system is paramount to make CCS affordable, especially for industrial (smaller) emitters
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THANK YOU
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QUESTIONS?
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BACKUP SLIDES
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Which transport solution to choose cost wise
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Transportation tariffs
5/13/2011 21From capture flange to storage well head; 20 year take or pay
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Transportation tariffs
5/13/2011 22From capture flange to storage well head; 20 year take or pay
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Transportation tariffs
5/13/2011 23From capture flange to storage well head; 20 year take or pay
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Transportation tariffs
5/13/2011 24From capture flange to storage well head; 20 year take or pay
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CO2 Hub Process Flow Diagram
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