michael tetteroo and cees van der ben - ccs projects – presentation at the global ccs institute...
TRANSCRIPT
Carbon IN TRAnsportLaunching project scheme
Implementation of LLSC study key findings
Melbourne October 4th, 2011
Cees van der Ben & Michael Tetteroo
This document and all information contained herein are the property
of
VOPAK, Anthony Veder, Gasunie & Air Liquide
and are Strictly Confidential
Note
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and are Strictly Confidential
It may not be copied or used without the written permission of
VOPAK, Anthony Veder, Gasunie & Air Liquide
Rotterdam Climate Initiative (RCI) city region CO2 reduction targets
-50%
vs 1990
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vs 1990
by 2025
� CCS plays a mayor role in the Dutch national reduction targets in general and in the Rotterdam targets in particular.
NW-Europe allows for short links between sources and sinks
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Several depleted gas fields become available and in due time incl. future aquifers: 50+ years of storage capacity for Europe.
Driving down costsSharing infra structure: simultaneously handling CO2
from multiple parties
Combining CO2 flows lies in the nature of CCS:
Power generation is responsible for 65%* of all green house gas emissionsPower generation is responsible for 65%* of all green house gas emissionsOECD/IEA Ref. Scenario 2006 2030
Total [TWh] 18921 33265 (+76%)
Coal 41% 44%
Nuclear 15% 10%
Renewables 18% 23%
���� Majority of sources are comparable regarding:
• Flow & conditions
• Compositions
• Characteristics
• Demands
*): Reference Scenario in 2005 & 2030: resp. 61% & 68 % in CO2 eq. terms
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)• Optimum CO2 : -50 ˚C, 7 bara
CINTRA’s CO2 Hub Partners
• Transport from the Emitters via pipelines or
barges
• Collection of CO2 to the CO2 Hub
• Loading of sea vessels / injection in trunk line
for transport to depleted offshore gas fields.
• Liquefaction at the Emitter’s
site or at the CO2 Hub
• Temporary Storage of CO2
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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/oil 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
• Temporary Storage of CO2
• Connecting Hub to offshore
trunk line or transfer to
vessel
CO2 Hub Concept Advantages
• Multiple emitters linked with multiple sinks , increasing reliability of CO2 take-away
• Modular design allows easy volume related ramp up
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• Variable destinations with liquid logistics
• Cost reduction through EOR
• Reduced project risk without onshore pipelines and onshore storage
How does it work
• MOVIE – will be shown during presentation
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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:multiple sources & sinks, both
12 2
3
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Sink 1 Sink 1Sink 3: EOR
at oil fieldSink 2 Sink n
small to justify off shore pipe
2. Intermediate scheme: two combined flows do allow for an off shore pipe => ship moves into alternative CO2 or LPG service
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
33
Potential CO2 Sinks
K12B300 Mton CO2
capacity
EORProjects
Other
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• First targeted sink: Dan Field Danish Continental Shelf, EOR Project Maersk Oil
• Hub forms a reliable CO2 source for EOR projects, allowing for a stable off take
• More contacts with other sink operators at the North Sea
• Potential CO2 from other ports will drive down costs for all participants further
Taqa
40 Mton CO2
capacity
CO2 from other ports
Rotterdam distance to sinks
• Dutch sinks are all within the 400 km range
• Rotterdam Ideally located
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• Rotterdam Ideally located for North Sea distribution
• Offshore EOR potential significant
CO2 HubLegal/Contractual Framework
Emitter Rotterdam Cintra Sink Operator
SH
Providing a One-Stop-Shop
SH SH SH
Transfer of CO2 title
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Emitter Rotterdam Cintra
Compression
& Transport
• CO2 title transfers from Emitter to sink Operator
• Transport organized via Service Level Agreements
LiquefactionBulk making
and terminal
Sea
Transport
Sink Operator
Necessary
sub-contracting
for other
specialized
services
CO2 HubLegal/Contractual Framework
• Emitters as CINTRA’s customers
• ETS allowances for Emitter
• CINTRA as multi-customer independent operator �no title to CO2
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no title to CO2
• CINTRA Transportation Agreements: long term take-or-pay contracts
• TA’s and SLA’s based on repeatable formula
• Impartiality and transparency towards customers
• CINTRA has one TA per emitter, backed up by one SLA per JV partner each
Stakeholder Management
Purpose:Purpose:mitigate risks associated with negative public perception for CCS
Type of Risks:Type of Risks:1. Negative image for companies involved2. Delay in time
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Steps to come to Stakeholder Strategy:Steps to come to Stakeholder Strategy:• Step 1: - Actor and network analysis• Step 2: - Inventarization communications and information options• Step 3: - Link actual communication option to key stakeholders• Step 4: - Execution in line with project development
2. Delay in time 3. Extra costs / investments to be made
beyond a first class SHE strategy
CO2 Hub Location
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Connecting HinterlandBarges to CO2 Hub
Hub
Emitter
Emitter
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• Liquefaction of CO2 at site
• River barges transport liquid CO2
over Rhine
• Cargoes from several sources can be
combined: economies of scale
• Capacity on Rhine is abundant vs.
pipeline hardly feasible
Emitter
Emitter
Current project status
• Launching emitters:– Coal fired power plant + post combustion capture 1.1 MTA– Hydrogen plant 0.4 MTA
• Launching sink: Maersk off shore EOR operation• Launching scope:
– On shore pipeline: 25 km, 40 bar– Terminal: 2.0 MTA liquefaction capacity, 20 kcbm LCO storage
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– Terminal: 2.0 MTA liquefaction capacity, 20 kcbm LCO2 storage– Ships: 2 x 12 kcbm with onboard conditioning equipment– Off loading: double buoy system
• Timing:– LOI’s in place: Q4 2011– FID: Q3 2012– RFO: Q2 2015– Challenge: synchronize timing & permitting
• Expected 2025 throughput: total 8 MTA of which 15 MTA via barge
Launching Scheme
Dan Field on the Danish sector of the North Sea is operated by Maersk Olie og Gas AS on behalf DUC – Dansk Undergrunds Consortium.
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Dan
CINTRA
• 1.5 MTA of CO2
• Rotterdam � Denmark• EOR
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 the
CO2 at the sourceSHE
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SHE• No items of concern encountered• Low vessel collision risk due to high LCO2 density• On shore pipeline through busy areas: 40 barCompression• Up to 100 bar: bull gear compressor ; beyond: pump• Moderate ambient temperatures: no power consumption difference
between conventional compression or compression/liquefaction/pumping.
Pipeline• In dense phase in order to minimize costs
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
Source: IEA GHG, 2004
Transportation Costs: insight evolution
LNG CO2
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CO2 CO2
GCCSI LLSC study lessons learned to date
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
• Combining multiple emitters in one system is paramount to make CCS affordable, especially for industrial (smaller) emitters
GCCSI LLSC studylessons learned to date
Legislation• Biggest remaining uncertainties:
– CO2 custody transfer: who, when and to whom– Monitoring requirements in the mean time
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 →
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• 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”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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• 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
The offshore scope - shipping
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10,000 cbm ship
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Distance [nm]• Loading & discharge 2000 t/hr• Sailing speed 15 kts• Voyage related spare 1 day
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Time line (years)
THANK YOU
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QUESTIONS?