Title: The Hydrogen Economy
1The Hydrogen Economy
Infrastructure Creation and End Use Application
- Jorge Plaza
- Scott Owens
- ChE 384
- November 21, 2006
2The Hydrogen Economy Its going to be a blast!!!!
3(No Transcript)
4Why H2ICE?
- ICE is a mature technology
- Near zero emissions
- High thermal efficiency
- LHV H2120 MJ/Kg Gasoline43 MJ/Kg
- H2 DI ICE is capable of 115 of the power of gas
ICE - Very tunable combustion
- LEL/UEL(Vol) H24/75 Gasoline 1/7.6
- Highly integrated designs possible
- Safe
5Variable Compression Ratios
6Safety
7Why NOT H2ICE?
Mass H2 Temp (K) Press (MPa) Vol (Gal L) EE Gas
1 Kg Atmos 25 16 60 1 gal
3.3 Kg 80 25 16 60 3.3 gal
lasts for 3 wks in tank.
8Why NOT H2ICE?
Material H-Atoms per cm3 (x 1022) wt hydrogen
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
- Storage Alternatives
- Alloy Hydrides
- Sodium Borohydride
- Liquid (infrastructure)
- High purity H2
- Non-Flammable
- Cost (80/kg)
- Weight (7wt loading)
- Recycle
9The Future Scenario
10The 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
11The Future Scenario
- Storage
- Solid Storage for small devices.
- Underground gaseous storage
- 2050 Carbon structures for storage.
12The 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
13Current 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
14Current Status
- Steam Methane Reforming
- Dependent on natural gas prices
- Connected to CO2 Sequestration
- Optimization
- Carbon/steam ratio
- Higher steam outlet temperature
- Catalysts
- Process configurations
15Current 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
16Current 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
17Current 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
18Current Status
- Coal Gasification
- Challenges
- CO2 sequestration
- Price dynamics
- Supply structure
- Alkaline Electrolysis
- Alkaline solution as electrolyte
19Current 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
20Current Status
21Current Status
- Solar and Nuclear
- Low peak generation
- Sulfur Iodine Process
- High temperature water splitting.
- Depend on development of Generation IV Nuclear
reactors - New materials for high temperature and corrosion
resistance. - Solar heat source
- Costs are not permissive
- Expected to be viable towards 2030
22Current Status
Method Description Challenges
Liquid hydrogen Available technology Use compressors and Heat exchangers 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
23Current Status
Method Description Challenges
Liquid hydrogen Double wall insulated tanks Trucks and barges or ships 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
24Conclusions
- 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.
25References
- Amendola, S.C., Sharp-Goldman, S.L., Janjua,
M.S., et al. A safe, portable, hydrogen gas
generator using aqueous borohydride solution and
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Efficiency and Low Emissions from a Port Injected
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415 March 13, 2006 - Changes in Vehicles per
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Hydrogen, Fuel Cells and Infrastructure
Technologies. Argonne National Laboratory.
26References Contd
- 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/st
r/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/c
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helle.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
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- Swain, M.R. Fuel Leak Simulation. University
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dfs/30535be.pdf - Turner J. Sustainable Hydrogen Production
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972 974. - U.S Department of Energy A National Vision of
Americas Transition to a Hydrogen Economy To
2030 and Beyond. Based on the results of the
National Hydrogen Vision Meeting. - US Department of Energy Project Update November
2006. FutureGen A Sequestration and Hydrogen
Research Initiative found at http//www.fossil.en
ergy.gov/programs/powersystems/futuregen/
27References Contd
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.pdf - http//www.princeton.edu/benziger/PEMFC.pdf