The Hydrogen Economy Infrastructure Creation and End Use Application Jorge Plaza Scott Owens ChE 384 November 21, 2006 The Hydrogen Economy: It’s going to be a blast!!!! CO2 Emissions by Source (1998) 500 MMTCE 400 300 200 100 0 Co al e El . c e c G as El Pe l E . rt o . c e In C . d l a o In G . d . as In d e P . tro a r T . s n O t r e h Why H2ICE? ICE is a mature technology Near zero emissions High thermal efficiency Very tunable combustion LHV: H2=120 MJ/Kg; Gasoline=43 MJ/Kg H2 DI ICE is capable of 115% of the power of gas ICE LEL/UEL(Vol%): H2=4/75; Gasoline =1/7.6 Highly integrated designs possible Safe Variable Compression Ratios Safety Why NOT H2ICE? One word - STORAGE: Mass H2 Temp Press (K) (MPa) 1 Kg 3.3 Kg Atmos 80 25 25 Vol EE Gas (Gal [L]) 16 [60] 1 gal 16 [60] 3.3 gal* *lasts for 3 wks in tank. Why NOT H2ICE? Storage Alternatives: Alloy Hydrides Sodium Borohydride Liquid (infrastructure) High purity H2 Non-Flammable Cost ($80/kg) Weight (7wt% loading) Recycle wt% hydroge n Material H-Atoms per cm3 (x 1022) H2 gas, 200 bar (2850 psi) .99 100 H2 liquid, 20 K (-253 C) 4.2 100 H2 5.3 100 MgH2 6.5 7.6 Mg2NiH4 5.9 3.6 FeTiH2 6.0 1.89 LaNi5H6 5.5 1.37 The Future Scenario The Future Scenario Production Similar timelines for Europe and US. Faster track for Europe. DOE expects feasibility determinations by 2015 Transition period where fossil fuels play major role. 2050 Europe – “de-carbonized” economy 2050 Centralized Production The Future Scenario Storage Solid Storage for small devices. Underground gaseous storage 2050: Carbon structures for storage. The Future Scenario Transportation Partial use of the natural gas grid reduces costs by 2010 Better liquefaction technology allows for trucks and ships Interconnected local grids by 2030 Current Status Production 40 million tons/ year Mainly natural gas reforming, coal gasification, water electrolysis. 95% SMR in the US Steam Methane Reforming Water + Methane feedstock Readily available Transition process Current Status Steam Methane Reforming Dependent on natural gas prices Connected to CO2 Sequestration Optimization: Carbon/steam ratio Higher steam outlet temperature Catalysts Process configurations Current Status Partial Oxidation Uses oxygen to convert into CO and H2 Expensive due to oxygen costs High operating temperatures Improvements in gas separation membranes may lower costs Current Status AutoThermal Reforming Blend of Partial Oxidation and SMR Very efficient process (93.9% theory) Smaller plants, faster start time Less mature technology Improvement in reactor design More resistant catalysts Current Status Coal Gasification Endothermic gasification No NOx concerns – low oxygen environment Integrated Gasification Combined Cycle Electricity and Hydrogen Efficiencies around 42% with hopes to 60% US Energy independence FutureGen Project Site selection by 2007 Online by 2012 Current Status Coal Gasification Challenges CO2 sequestration Price dynamics Supply structure Alkaline Electrolysis Alkaline solution as electrolyte Current Status Alkaline Electrolysis Efficiencies, lifetime and costs. High Temperature and pressure electrolyzers Polymer Electrolyte Membrane Recent technology Polymer membrane as electrolyte Operation at high pressures High cost of membranes and electrodes Current Status Biomass Production Current Status Solar and Nuclear Low peak generation Sulfur – Iodine Process Solar heat source High temperature water splitting. Depend on development of Generation IV Nuclear reactors New materials for high temperature and corrosion resistance. Costs are not permissive Expected to be viable towards 2030 Storage Method Current Status Description Liquid hydrogen •Available technology •Use compressors and Heat exchangers Challenges •High compression costs •Prevention of boil-off Compressed Gas •Available Technology •Use of caverns for large scale long timeframe •Compression costs for vessel storage •Inefficient unloading Metal Hydride •Chemically bonded hydrogen •High pressure release •Infant technology •Hydride storage capacity •Hydride stability Current Status Transportation Method Description Liquid hydrogen •Double wall insulated tanks •Trucks and barges or ships Challenges •Cost •Boil-off rates Compressed Gas •Mainly pipelines •May use part of the natural gas infrastructure •Operational and capital costs •Hydrogen embrittlement Metal Hydride •Containers with the hydride are switched or unloaded at site. •Cost of the containers for hydride transportation Conclusions Strong need for a clear public policy Further optimization of available technologies is required Work is needed in the whole hydrogen supply infrastructure “No silver bullet” . Hydrogen is an option First sight around 2020. References Amendola, S.C., Sharp-Goldman, S.L., Janjua, M.S., et al. “A safe, portable, hydrogen gas generator using aqueous borohydride solution and Ru catalyst.” International Journal of Hydrogen Energy 25. Elsevier Science Ltd, 2000. http://www.obitet.gazi.edu.tr/makale/internalcombustionengines/021.pdf Amos W. “Cost of Storing and Transporting Hydrogen”. National Renewable Energy Laboratory. NREL/TP-570-25106. November 1998. 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References Cont’d Powers, Laurie. “Flexibly Fueled Storage Tank Brings hydrogen Powered Cars Closer to Reality.” Lawrence Livermore National Lab (LLNL), Department of Energy 2003. http://www.llnl.gov/str/June03/Aceves.html Roberts, Paul. The End of Oil. Houghton Mifflin Company. Boston, MA. 2004. Rochelle, G.T., “Presentation Made to Prospective Grad Students, 2005.” http://www.engr.utexas.edu/che/students/graduate/05_graduate_presentations/Rochelle.ppt Schatz Energy Research Center, Humboldt State University. “Development of a PEM Electrolyzer: Enabling Seasonal Storage of Renewable Energy –Feasibility and Final Energy Innovations Small Grant Report” Prepared for the California Energy Commission. May 2005 Sandia National Lab, United States Department of Energy. A. hydrogen Research Program http://www.ca.sandia.gov/hydrogen/index.html B. Combustion Research Facility http://www.ca.sandia.gov/crf/research/combustionEngines/PFI.php Swain, M.R. “Fuel Leak Simulation.” University of Miami. 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