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CO2 from Natural Gas Sweetening to Kick-Start EOR in the North Sea 
Marit J. Mazzettia, Ragnhild Skagestadb, Anette Mathisenb, Nils H. Eldrupb 
Marit.Mazzetti@sintef.no 
Nordic CCS Competence Centre
Sweetening the deal for CCS 
• 
For some fields Gas Sweetening is used to remove CO2 from natural gas before export 
• 
Some not yet developed oil and gas fields at Utsira/Barents Sea/Northern Norway have CO2 levels >2,5% 
• 
Steady supply of CO2 which is necessary to start an EOR project 
• 
Location onshore close to ‘source & sink’ 
• 
Economies of scale significant for volumes of CO2 captured of up to 2-3 Mt/year
A selection of NCS wellbores on the NCS with CO2 content above 5% 
Based on data from NPD fact pages, adapted from CO2 Storage Atlas Norwegian North Sea[1] (Vinni and Njord in Norskehavet outside Trondheim, West Vanguard - off coast of Lofoten in Northern Norway) 
25 fields CO2 >5% 8 fields CO2 >10
MDEA Sweetening Process 
New MDEA plant at Generic Site 
• 
CO2 in feed 10% 
• 
Reduce CO2 to 2.5% 
• 
compress CO2 to 70 bar 
• 
optimal site onshore 
• 
shortest possible distance for CO2 transport to storage or EOR site 
Natural Gas Composition 
Inlet values 
(mol %) 
Mass flow in 
(tonne/h) 
Mass flow out 
(tonne/h) 
CH4 
83.6 
567 
567 
CO2 
9.9 
186 
55 
H2O 
6.3 
48 
2 
Pressure (bar) 
70 
Temperature (C) 
40 
Economic parameter 
Value 
Unit 
Rate of return 
7 
% 
No of operating years 
23 
years 
Construction time 
Capture cost 
2 
Year 
Not avoided cost
Cost CAPEX and OPEX Nth of a kind plant 
Location CAPEX (k€) OPEX (k€/yr) Capture Cost (€/ton) Generic location 60000 33272 34.2 Remote location 90000 34470 37.8
Cost Savings Nth of a kind Plant 
• 
Cost is 30% lower than the cost of the conventional amine MEA technology for CO2 capture from flue gas 
• 
Norway: Combined CO2 taxes and ETC total 55€/tonne
Cost of different NORDICCS Case Scenarios - Nth of a kind (NOAK) Capture Technology
Kick-start CCS 
• 
CCS project with natural gas sweetening/EOR shows promising economy 
– 
Removal cost from natural gas 30% lower than from flue gas 
– 
Potential additional cost reduction from use of CO2 for EOR 
• 
Steady supply of CO2 needed to kick-start deployment of CCS 
– 
Central hub for CO2 
– 
CO2 EOR at a nearby oil field 
•Create a market for CO2 for land-based industry 
– allowing start of industrial CCS projects.
Acknowledgements/Thank You/Questions 
• 
This work is supported by the NORDICCS Centre, performed under the Top-level Research Initiative CO2 Capture and Storage program, and Nordic Innovation. 
• 
The authors acknowledge the following partners for their contributions: Statoil, Gassco, Norcem, Reykjavik Energy, CO2 Technology Centre Mongstad, Vattenfall and the Top-level Research Initiative 
(Project number 11029)

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CO2 from Natural Gas Sweetening to Kick-Start EOR in the North Sea

  • 1. CO2 from Natural Gas Sweetening to Kick-Start EOR in the North Sea Marit J. Mazzettia, Ragnhild Skagestadb, Anette Mathisenb, Nils H. Eldrupb Marit.Mazzetti@sintef.no Nordic CCS Competence Centre
  • 2. Sweetening the deal for CCS • For some fields Gas Sweetening is used to remove CO2 from natural gas before export • Some not yet developed oil and gas fields at Utsira/Barents Sea/Northern Norway have CO2 levels >2,5% • Steady supply of CO2 which is necessary to start an EOR project • Location onshore close to ‘source & sink’ • Economies of scale significant for volumes of CO2 captured of up to 2-3 Mt/year
  • 3. A selection of NCS wellbores on the NCS with CO2 content above 5% Based on data from NPD fact pages, adapted from CO2 Storage Atlas Norwegian North Sea[1] (Vinni and Njord in Norskehavet outside Trondheim, West Vanguard - off coast of Lofoten in Northern Norway) 25 fields CO2 >5% 8 fields CO2 >10
  • 4. MDEA Sweetening Process New MDEA plant at Generic Site • CO2 in feed 10% • Reduce CO2 to 2.5% • compress CO2 to 70 bar • optimal site onshore • shortest possible distance for CO2 transport to storage or EOR site Natural Gas Composition Inlet values (mol %) Mass flow in (tonne/h) Mass flow out (tonne/h) CH4 83.6 567 567 CO2 9.9 186 55 H2O 6.3 48 2 Pressure (bar) 70 Temperature (C) 40 Economic parameter Value Unit Rate of return 7 % No of operating years 23 years Construction time Capture cost 2 Year Not avoided cost
  • 5. Cost CAPEX and OPEX Nth of a kind plant Location CAPEX (k€) OPEX (k€/yr) Capture Cost (€/ton) Generic location 60000 33272 34.2 Remote location 90000 34470 37.8
  • 6. Cost Savings Nth of a kind Plant • Cost is 30% lower than the cost of the conventional amine MEA technology for CO2 capture from flue gas • Norway: Combined CO2 taxes and ETC total 55€/tonne
  • 7. Cost of different NORDICCS Case Scenarios - Nth of a kind (NOAK) Capture Technology
  • 8. Kick-start CCS • CCS project with natural gas sweetening/EOR shows promising economy – Removal cost from natural gas 30% lower than from flue gas – Potential additional cost reduction from use of CO2 for EOR • Steady supply of CO2 needed to kick-start deployment of CCS – Central hub for CO2 – CO2 EOR at a nearby oil field •Create a market for CO2 for land-based industry – allowing start of industrial CCS projects.
  • 9. Acknowledgements/Thank You/Questions • This work is supported by the NORDICCS Centre, performed under the Top-level Research Initiative CO2 Capture and Storage program, and Nordic Innovation. • The authors acknowledge the following partners for their contributions: Statoil, Gassco, Norcem, Reykjavik Energy, CO2 Technology Centre Mongstad, Vattenfall and the Top-level Research Initiative (Project number 11029)