Hydrogen Production from Biogas by Sorption-Enhanced Steam Methane Reforming (SE-SMR)

Hydrogen Production from Biogas by Sorption-Enhanced Steam Methane Reforming (SE-SMR)

Hydrogen Production from Biogas by Sorption-Enhanced Steam Methane Reforming (SE-SMR) Demonstration of the Novel Process at the HyNor Lillestrøm Hydrogen Station Julien Meyer, Johann Mastin, Roger Smeets Institute for Energy Technology (IFE) Department of Environmental Technology www.ife.no; [email protected] TCCS-6, Trondheim, 14-16 june 2011 Outline • The HyNor project • The HyNor hydrogen station at the city of Lillestrøm • The Sorption-Enhanced Steam Methane Reforming process (SE-SMR) for hydrogen production with integrated CO2-capture • The SE-SMR pilot unit planned at the Hynor Lillestrøm station TCCS-6, Trondheim, 14-16 june 2011 The HyNor project The hydrogen “highway” in Norway www.hynor.no • Demonstration of hydrogen production technologies for the introduction of hydrogen as transportation fuel in Norway • Make possible driving between the cities of Oslo and Stavanger with hydrogen vehicles • Sweden, Danmark and Germany also have similar hydrogen road projects • Hydrogen Sweden • Hydrogen Link • Clean Energy Partnership (CEP) TCCS-6, Trondheim, 14-16 june 2011 The HyNor Lillestrøm project www.hynor.no/romerike http://hynor-lillestrom.no Lillestrøm • Hydrogen production based on renewable energy • From landfill gas produced at a nearby landfill and transported by pipe to the station • From electrolysis using power from the grid and from photovoltaic panels installed at the station • Hydrogen compression to 700 bar • Conventional mechanical compression • Demonstration of a metal hydride compressor delivering at 200 bar • On-site hydrogen delivery (dispenser) • Hydrogen vehicles fleet: 4 Think Hydrogen TCCS-6, Trondheim, 14-16 june 2011 Project participants and financing • Hynor Lillestrøm AS: project owner • Institute for Energy Technology (IFE): project leader • Akershus Energi AS: building and infrastructure • Technology suppliers • IFE: Reformer unit and system integration • HyGear: Landfill gas upgrader and hydrogen purification • H2-Logic: Electrolyzer, compression & storage system, dispenser • Hystorsys: Metal hydride compressor • Scandpower AS: Risk analysis and safety • Financed by • Akershus County (Akershus Fylkeskommune) • Research Council of Norway through the Renergi-program • Transnova (governmental trial funding program) • Innovation Norway TCCS-6, Trondheim, 14-16 june 2011 http://www.aeas.no/pages/akershus-energipark TCCS-6, Trondheim, 14-16 june 2011 The Akershus Energy park Service Building / R&D Building / Training Center Hydrogen Station Energy Plant 2009 2010 Last quarter of 2011 TCCS-6, Trondheim, 14-16 june 2011 The HyNor building and hydrogen station HyNor Lillestrøm AS: Akershus Energy AS: Demonstration Projects Research Projects • Hydrogen Production • Renewable Energy • Hydrogen Compression Hydrogen Refuelling Hydrogen Fuel Cell Vehicles TCCS-6, Trondheim, 14-16 june 2011 HyNor Lillestrøm System Concept • Production capacity 3 • 10 Nm /h H2 from the electrolysis line 3 • 10 Nm /h H2 from the reforming line • Purity of 99.99% minimum TCCS-6, Trondheim, 14-16 june 2011 The reformer unit TCCS-6, Trondheim, 14-16 june 2011 Sorption enhanced steam methane reforming H2-production with integrated CO2-capture in one single step Reforming CH4 (g) + H2O (g) CO (g) + 3H2 (g) Water gas shift CO (g) + H2O (g) CO2 (g) + H2 (g) Carbonation CaO (s) + CO2 (g) CaCO3 (s) Total reaction (SE-SMR) CaO (s) + CH4 (g) + 2H2O (g) CaCO3 (s) + 4H2 (g) Calcination (regeneration) CaCO3 (s) CaO(s) + CO2 (g) TCCS-6, Trondheim, 14-16 june 2011 Sorption enhanced steam methane reforming Principle and basic concept TCCS-6, Trondheim, 14-16 june 2011 Sorption Enhanced Steam Methane Reforming Advantages of the novel H2-production route • Higher H2-yields (95% +) than in conventional SMR, in one single step, and at lower temperature (500-600 C) • Simplified process layout (fewer vessels) • No need for shift catalyst • Reduced needs for downstream H2-purification • Potential for lower production costs and energy savings TCCS-6, Trondheim, 14-16 june 2011 Reactor technology • Fluidized bed reactor technology • Liquid like behaviour makes Reformate transport of solids possible Top cyclone • Very good heat transfer CO2/steam Hopper Circulation valve Make-up tank REG cyclone Make-up tank (catalyst) • Dual bubbling fluidized bed (dolomite) REF cyclone reactor (DBFB) Exhaust gas Riser HP-E13 X Regenerator • 2 dedicated reactors connected with Loop seal Burner exhaust ags loop seals and transport riser Regenerator • Continuous mode Loop-seal Purge tank Steam Reformer • Bubbling regime Reformer feed • Circulation rate regulated with a slide valve • High temperature tube heat exchanger in the regenerator TCCS-6, Trondheim, 14-16 june 2011 Simplified SE-SMR process Reformate gas CO2 stream Top cyclone CO2 sorbent Catalyst tank tank Air 850oC Burner section 600oC Burner HT Bag filter Purge tank Regenerator feed gas Reformer feed gas Reactor section Hydrogen Steam Steam Exhaust gas Upgraded biogas Off-gas buffer tank PSA section Reformate Compressor PSA off-gas buffer tank Sep. Sep. PSA Pure hydrogen to compression Dryer CO2 stream Condensate Condensate TCCS-6, Trondheim, 14-16 june 2011 Experimental results Bubbling bed batch reformer/regenerator Batch FB-reformer at IFE TCCS-6, Trondheim, 14-16 june 2011 The DBFB SE-SMR pilot • H2 production capacity • 12.5 Nm3/h • Reformer • 625oC; 0.5-1 barg • 0.29 m/s; S/C ratio: 4 • Upgraded biogas (Swedish standard) • Regenerator • 850oC; 0.5-1 barg • 0.10 m/s • Steam + 2 vol% hydrogen • Solids • Arctic dolomite from Franzefoss • 200µm • Commercial reforming catalyst • 150µm • Ratio sorbent/catalyst: 2.5 – 3 w/w • Solids circulation rate: 75 kg/h • Installation in the last quarter of 2011 • Testing and commissioning in first quarter of 2012 TCCS-6, Trondheim, 14-16 june 2011 Other applications of the SE-SMR process Power production and co-production • H2-production with CO2-capture and steam boilers • H2-production with CO2-capture and CC power plant • H2-production with CO2-capture and SOFC • ZEG-Power concept • Co- production of electricity and hydrogen with integrated CO2- capture • Electricity from high temperature solid oxide fuel cells (SOFC) • Hydrogen production by sorption enhanced steam methane reforming • High total energy efficiency TCCS-6, Trondheim, 14-16 june 2011 Thank you for your attention ! TCCS-6, Trondheim, 14-16 june 2011 .

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