CCUS CRITICAL FOR CARBON NEUTRALITY David Nevicato CCUS
CCUS CRITICAL FOR CARBON NEUTRALITY David Nevicato CCUS R&D program
OUR CHALLENGES Meeting the Energy Needs of a Growing Population Contributing to limit Global Warming Continually Reinventing the Customer Relationship Dîner-débat UNAFIC- 26 novembre 2019 2
REDUCING CARBON INTENSITY OF OUR ENERGY SALES Responsible contribution to tackle climate challenge Carbon intensity Base 100 in 2015 (75 g. CO 2/kbtu) Realized Ambition -15% 2015 -30 100 95 85 75 60 50 2015 2018 2030 2040 CO 2 Ship transport - METI & TOTAL - 28. 10. 2019 3
CCUS – A PRAGMATIC APPROACH Source: US DOE / NETL (National Energy Technology Laboratory), Cost and Performance Baseline for Fossil Energy Plants, Revision 3, July 2015 ● CCU and CCS both contribute to capture technology development and necessary costs reductions ● Storage: necessary for CO 2 sinks, and a Source: ZEP “Climate solutionsfor EU industry: interaction between electrificatio n, CO 2 use and CO 2 storage”. permanent solution for large volumes of residual CO 2 (cement, steel, etc. ) ● Utilization has far less volume potential (case specific, R&D efforts required) Dîner-débat UNAFIC- 26 novembre 2019 4
OUR CCUS AMBITION To have CCUS globally recognized leadership by 2035 To provide our customer a CCUS solution towards carbon neutrality. To prepare for new business opportunities. ● One R&D strategy for CCUS ● R&D key enabling factors 1. To reduce CCS Cost • Optimize mature technologies thought scale-up effect • Promote technologies competition • Push disruptive technologies to the market 2. To evaluate mass market opportunities in CO 2 Utilization 3. To be present all along the value chain of CCUS • Take part in industrial projects • Create new business models 4. To scale-up CCUS impact on Climate • Derisk mega CO 2 storage capacities Dîner-débat UNAFIC- 26 novembre 2019 - Work for CCUS sustainability - Develop internal expertise - Leverage our impact through OGCI and through partnership funding Worldwide involvement : USA, EU, Asia, Middle East 5
OVERVIEW OF EXISTING AND PLANNED CCS PROJECTS IN EUROPE Source: IOGP June 2019 Dîner-débat UNAFIC- 26 novembre 2019 6
NORTHERN LIGHTS PROJECT (operator) Northern Lights, CO 2 shipping and storage part of the first full-chain CCS commercial project based upon multiple industrial CO 2 emissions. ⅓ ⅓ Project design capacity 1. 5 MTPA (1 st phase) Offshore pipeline designed for 5 MTPA 1 ü MAX 0. 8 MTPA estimated State reserved capacity for volumes from capture sites in the Oslo area : Troll AURORA 110 km of 12” sealine (Capacity : 5 MTPA) Naturgassparken Bergen Fortum Oslo 1 -2 injector wells WD 300 m TVD 3000 m Norcem Well spud on November 1 st Capture 600 km Unloading of > 99% Liq CO 2 MP option : 15 b, -30°C Analog LPG ship design, 2 x 7. 500 m 3 à Enabling low carbon industry and CO 2 sinks • Fortum, waste incinerator FEED phase CO 2 capture : 0. 4 MTPA • Norcem, cement factory FEED phase CO 2 capture : 0. 4 MTPA ü MIN 0. 7 MTPA available capacity to market Northern Lights : shipping / storage operator 3 Storage 2 Dîner-débat UNAFIC- 26 novembre 2019 Shipping 7 ⅓
SPEED-UP CO 2 CAPTURE BREAKTHROUGH TECHNOLOGIES TO MARKET WITH Pilot unit Lacq Research Center OGCI-CI Investment Demonstration Unit to CO 2 EOR/Storage CCUS Innovation Cluster : CO 2 MENT Project (0, 9 M$) 30 TPD CO 2 0. 1 TPD CO 2 2 TPD CO 2 CAPTURE on cement kiln Dîner-débat UNAFIC- 26 novembre 2019 CO 2 to cement and concrete 8
SET UP DEMO PLANT – LACQ PLATFORM Adsorption Pilot unit 0. 1 TPD CO 2 30 TPD CO 2 Dîner-débat UNAFIC- 26 novembre 2019 9
CHEERS PROJECT : CHEMICAL LOOPING COMBUSTION CHEERS = CHinese-European Emission-Reducing Solutions Reduced metallic oxide ● ● OOO OO Metallic oxide N≡N Nitrogen H HCH H Fuel OC O Carbon dioxide HOH water Combustion process with inherent CO 2 capture high energy efficiency Feed: mainly solid fuel Products: steam, electricity, possibly N 2 CO 2 output : geological storage, EOR, use Dîner-débat UNAFIC- 26 novembre 2019 10
CHEERS PROJECT : CHEMICAL LOOPING COMBUSTION International pioneer in retrofitting an existing unit to CLC Demonstration of CLC technology with solid fuel In the frame work of Horizon 2020 Work Program and China MOST Quality of CO 2 based on EOR requirements Techno-economic evaluation of industrial scale unit 3 MWth scale Oct 17: Pre-Feed Mars 19: FEED, LLI procurement June 20: EPC Dîner-débat UNAFIC- 26 novembre 2019 March 21: Operation and testing 11
CCUS VALUE CHAIN DEVELOPMENT - STEEL PLANT 3 D project : DMXTM Demonstration in Dunkirk CO 2 Cluster : 12 Mt CO 2/y that could be captured in a short term DMXTM Demonstration Unit in Arcelor Mittal Steel Plant 3 D project received funding from the European Union’s Horizon H 2020 research and innovation programme under grant agreement No 838031 Dîner-débat UNAFIC- 26 novembre 2019 12
CCUS VALUE CHAIN DEVELOPMENT - STEEL PLANT Dîner-débat UNAFIC- 26 novembre 2019 13
COMPARISON OF CO 2 UTILIZATION TECHNOLOGIES REQUIRED Indirect two-step synthesis of olefins and alcohols (via H 2 with low/no CO 2 footprint) Alcohols Totals MTO-OCP Process Direct electrocatalytic synthesis of olefins and alcohols CO 2 to polymers Polymers CO 2 mineralization CO 2 stored Olefins Polymerizatio n Techno-economic and life cycle analysis Dîner-débat UNAFIC- 26 novembre 2019 14
COMPARISON OF CO 2 UTILIZATION TECHNOLOGIES REQUIRED Indirect two-step synthesis of olefins and alcohols (via H 2 with low/no CO 2 footprint) Alcohols Totals MTO-OCP Process Direct electrocatalytic synthesis of olefins and alcohols CO 2 to polymers Polymers CO 2 mineralization CO 2 stored Olefins Polymerizatio n Techno-economic and life cycle analysis Dîner-débat UNAFIC- 26 novembre 2019 15
COMPARISON OF CO 2 UTILIZATION TECHNOLOGIES REQUIRED Indirect two-step synthesis of olefins and alcohols (via H 2 with low/no CO 2 footprint) Alcohols Totals MTO-OCP Process Direct electrocatalytic synthesis of olefins and alcohols CO 2 to polymers Polymers CO 2 mineralization CO 2 stored Olefins Polymerizatio n Techno-economic and life cycle analysis Dîner-débat UNAFIC- 26 novembre 2019 16
COMPARISON OF CO 2 UTILIZATION TECHNOLOGIES REQUIRED Two-step CO 2 conversion Indirect two-step synthesis Thermo-catalytic Electro-catalytic of olefins and alcohols CO 2 hydrogenation water electrolysis (via H 2 with low/no CO 2 footprint) + H 2 Alcohols One-step CO 2 conversion Direct electrocatalytic Electrocatalytic CO 2 reduction synthesis of olefins and alcohols + Totals MTO-OCP Process Olefins Polymerizatio n + CO 2 to polymers Polymers CO 2 mineralization CO 2 stored Techno-economic and life cycle analysis Dîner-débat UNAFIC- 26 novembre 2019 17
COMPARISON OF CO 2 UTILIZATION TECHNOLOGIES REQUIRED Two-step CO 2 conversion Indirect two-step synthesis Thermo-catalytic Electro-catalytic of olefins and alcohols CO 2 hydrogenation water electrolysis (via H 2 with low/no CO 2 footprint) + H 2 Alcohols One-step CO 2 conversion Direct electrocatalytic Electrocatalytic CO 2 reduction synthesis of olefins and alcohols + Totals MTO-OCP Process Olefins Polymerizatio n + CO 2 to polymers Polymers CO 2 mineralization CO 2 stored Techno-economic and life cycle analysis Dîner-débat UNAFIC- 26 novembre 2019 18
RECYCLING CO 2 : E-CO 2 MET PROJECT IN LEUNA Power generation Integrated demonstration unit for electrolysis & methanol synthesis Renewable Electricity ew Water Me. OH H 2 N lid o S ! e id x o Heat Electrolysis H 2 for energy storage ! O 3 w n 2 e I N st ly a t a C H 2 O Heat Chemical conversion Industrial 94% CO 2 Dîner-débat UNAFIC- 26 novembre 2019 19
CO 2 GEOLOGICAL STORAGE STAKES Geological CO 2 storage represents today the only way to remove large CO 2 emissions from the atmosphere. Status Today: Since 2000’s, several million tons (Mt) per year scale CO 2 storage projects have been done and demonstrated the feasibility of the tool: • • Sleipner and Snovit in Norway (1. 7 Mt. CO 2/y), Illinois Basin-”Decatur” in USA (1. 0 Mt. CO 2/y), Quest in Canada (1. 2 Mt. CO 2/y), Gorgon in Australia (4. 0 Mt. CO 2/y), What is new ? Need for scale-up: In order to significantly reduce global CO 2 emissions, the goal of the next decades would be to scale up and demonstrate the feasibility of gigatonnes (Gt) per year scale projects. Dîner-débat UNAFIC- 26 novembre 2019 20
SUSTAINABLE CCUS PROJECT Dîner-débat UNAFIC- 26 novembre 2019 21
MULTI SCALE SUSTAINABILITY Economics • Initial cost estimate • TEA technology Component • Eng & Proc. Cost Environment Acceptability • Input / output • Eco-design • Risk analysis • Monitoring technologies System • LCOx • Architecture • Financing • LCA project and systems • Benchmark • Integrated risk plan • Codevelopment approach Society • Bankability • Policies • CO 2 pricing • IAMs with natural resources and climate • Value of CCUS • Company engagement Dîner-débat UNAFIC- 26 novembre 2019 22
TOTAL LEADER IN CCUS VALUE CHAIN BY 2035 Decrease technologies Improve our Contrib To DECREASE CCUS TECHNOLOGIES COST C C U S ost arbon footprint te to a more favorable development context ustain our activities in the future DECREASE GLOBAL CARBON FOOTPRINT Dîner-débat UNAFIC- 26 novembre 2019 INCREASE CCUS SOCIAL ACCEPTABILITY 23
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