Demonstration of oxy-fuel combustion in once-through steam generators for CO 2 capture Carbon Capture & Storage Workshop 28 March, 2013 The High Commission.

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Presentation transcript:

Demonstration of oxy-fuel combustion in once-through steam generators for CO 2 capture Carbon Capture & Storage Workshop 28 March, 2013 The High Commission of Canada, Canada House, London Prepared by: Mark Bohm (Suncor) Capture Team Member Mark Crombie (BP): CCP3 Program Manager Presented by: Mark Crombie (BP): CCP3 Program Manager

The CO 2 Capture Project (CCP) is an award-winning partnership of several major energy companies working to advance the technologies that will underpin the deployment of industrial-scale CO 2 capture and storage (CCS). The CCP is currently in its third phase of activity: CCP Project Overview Phase 1 (CCP1, ) technology screening/proof of concept – completed Phase 2 (CCP2, ) intensive development – completed Phase 3 (CCP3, ) demonstration – on going The CCP is funded primarily by: Member contributions Government grants In-kind contributions

3 CCP Mission Statement “To develop technologies that will reduce the risks of and further advance CO 2 capture and geological storage; making CCS a practical reality for atmospheric carbon mitigation” How does CCP work? Collaboration of leading oil & gas companies, government, NGOs, academic institutions, Current members are BP, Chevron, ENI, Petrobras, Shell and Suncor Over 200 joint projects to date, broad scope ranging from policy to technology development, R&D and knowledge sharing Incorporates oil & gas industry expertise + power industry experience CCP is now a leading authority on CCS, sharing research findings

4 OTSG - Importance of Capture Solution 80-85% of oil sands are currently accessible only through in-situ production methods; these are less invasive than mining and with a smaller environmental footprint SAGD is the leading technology, but is more energy and GHG intensive because of the large steam requirements Current carbon emissions from SAGD facilities exceed 25 Mt/yr, and are expected to be the oil sand sector’s largest source of future emission growth A cost-effective solution for CO 2 capture from once-through steam generators (OTSG) is needed for both greenfield and retrofit applications CCP and its Partners recognize the importance of an economic, retrofitable CCS solution for OTSGs

5 Unparalleled Project Team Expertise Project Lead: Suncor Funding Partners: Cenovus Energy (host site), CO 2 Capture Project, Devon, Praxair, Statoil, MEG Energy Technology Providers: Praxair – industrial gas & combustion technology

6 Potential CCS Solutions for OTSGs Requires solvents; potential source of secondary emissions 90% Capture rate Large steam requirements Commercially available No solvents needed; near zero emissions 99% Capture rate Requires power Need to demonstrate oxy-fuel burners and CO 2 purification AminesOxy-fuel

7 Oxy-fuel Technology for OTSGs Key Technologies ASU – Air Separation Technology CPU – CO 2 Separation and Compression Technology Large Plant Engineering (Design, Construct, Operate, Maintain) Oxy-Fuel Combustion Technology Safety, System Integration and Optimization Fuel Flue Gas Recirculation OTSG-Boiler Flue gas (CO 2 -rich) CO 2 Processing Unit (CPU) Vent of Non-Condensable Gases ( N 2, Ar, excess O 2 ) CO 2 Water Oxygen Air Nitrogen Air Separation Unit (ASU) Key to Success: Integration and Optimization of Existing Technologies

8 Overview of Project Three Phase Project: Phase I (completed): Develop design basis and cost estimates for test and commercial scale OTSG Phase II (2013): Pilot oxy-fuel combustion on 50 mmbtu/hr test boiler Phase III (2014+): Pilot oxy-fuel combustion, compression and purification on test boiler Overall Objective: To demonstrate that oxy-fuel combustion is a safe, reliable and cost-effective technology for CO 2 capture from once-through steam generators

9 Phase II - Oxy-fuel Boiler Test Existing commercial OTSG Boiler at Cenovus Energy - Christina Lake Retrofit with flue gas recirculation Installation of oxygen supply and control integration Flue Gas Recirculation FGR Damper Air ~95% CO 2 + H 2 O Oxygen (gas) Liquid Oxygen Feedwater Natural Gas OTSG-Boiler Steam Air Damper FD-Fan EvaporatorEco Flue gas Project will demonstrate technical viability and safety of oxy-fuel combustion at operating in-situ site

10 Oxy-Fuel Technology Challenges Net Heat Flux on Boiler Tubes (W/m 2 ) Air Baseline Gas Temperature ( o F) Heat transfer changes in boiler versus air combustion Burner design for desirable flame shape and stability Material temperature limits, scale-up, emissions Startup, operation, boiler performance and controls 140,00002,0001,000 Oxy-fuel - Mixture of FGR and Oxygen

11 Oxy-Fuel Burner Designs Oxygen Mixer uses existing Coen burner → potential limitations on flame stability and heat transfer profile Oxygen Natural Gas Flue Gas Recirculation Existing Air Burner Oxygen Sparger to mix oxygen into FGR Oxygen Natural Gas Flue Gas Recirculation Existing Opening A-Burner with new burner block Flue Gas Recirculation Natural Gas Oxygen Existing Opening JL-Burner with new burner block A-Burner high degree of flame and heat transfer adjustment water cooled JL-Burner very simple design need to prove operation at commercial scale

12 Technical Demonstration Goals Establish operating parameters for oxy-fuel combustion applied to SAGD boilers (heat transfer, steam flow and quality) Confirm CFD model predictions with test results Identify and understand scale-up issues and retrofit risks Startup and control boiler to suit process needs Verify boiler NOx emissions with test measurements Goal: Reliable Oxy-fuel Operation with known capture costs

13 Project Summary Project addresses significant and growing source of GHG emissions in Alberta CO 2 capture is an option as large facilities exist (for retrofits or greenfield) Strong Group of Committed Participants Consortium of energy companies working towards a common solution World leading technology providers Compelling Technology Solution Oxy-fuel combustion with flue gas purification is expected to have a cost advantage over amine systems Applicable to other combustion sources including upgrading and refining

14 Thank You Mark Bohm, P.Eng Suncor Energy Tel: Mark Crombie, MBA BP Alternative Energy Tel: