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The Hydrogen Economy

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Title: The Hydrogen Economy


1
The Hydrogen Economy
Infrastructure Creation and End Use Application
  • Jorge Plaza
  • Scott Owens
  • ChE 384
  • November 21, 2006

2
The Hydrogen Economy Its going to be a blast!!!!
3
(No Transcript)
4
Why 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

5
Variable Compression Ratios
6
Safety
7
Why NOT H2ICE?
  • One word - STORAGE

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.
8
Why 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

9
The Future Scenario
10
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

11
The Future Scenario
  • Storage
  • Solid Storage for small devices.
  • Underground gaseous storage
  • 2050 Carbon structures for storage.

12
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

13
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

14
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

15
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

16
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

17
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

18
Current Status
  • Coal Gasification
  • Challenges
  • CO2 sequestration
  • Price dynamics
  • Supply structure
  • Alkaline Electrolysis
  • Alkaline solution as electrolyte

19
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

20
Current Status
  • Biomass Production

21
Current 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

22
Current Status
  • Storage

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
23
Current Status
  • Transportation

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
24
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.

25
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/internalcombu
    stionengines/021.pdf
  • Amos W. Cost of Storing and Transporting
    Hydrogen. National Renewable Energy Laboratory.
    NREL/TP-570-25106. November 1998.
  • Becker, Laura. Hydrogen Storage. CSA,
    Materials Information Metals, Engineered
    Materials, Aluminum Industry and Corrosion
    Abstracts. 2001. http//www.csa.com/discoverygui
    des/hydrogen/overview.php
  • Brusstar, M., Stuhldreher, M., Swain, D. High
    Efficiency and Low Emissions from a Port Injected
    Engine with Neat Alcohol Fuels. United States
    EPA and Society of Automotive Engineers.
    2002.http//www.epa.gov/OMS/presentations/sae-200
    2-01-2743.pdf
  • Chen T. Investigation of Catalytic Autothermal
    Reforming Process for Hydrogen Production.
    Proceedings of the Taiwan Tech Trek 2005 Academic
    Conference. Taipei, Taiwan.
  • Energy Efficiency and Renewable Energy (EERE)
    United States Department of Energy. A. Fact
    415 March 13, 2006 - Changes in Vehicles per
    Capita around the World. 2006.
    http//www1.eere.energy.gov/vehiclesandfuels/facts
    /2006_fcvt_fotw415.htmlB. hydrogen
    Infrastructure and Technologies Program 2006.
    http//www.eere.energy.gov/hydrogenandfuelcells/pr
    oduction/
  • Foster Wheeler. Hydrogen Plants for the New
    Millennium. Presented at the Middle East
    PETROTECH 2001. Bahrain, October 29-31 2001.
  • Green Car Congress. The Arguments for hydrogen
    Combustion Engines. 2006. http//www.greencarcon
    gress.com/2006/09/the_arguments_f.html
  • International Energy Agency Organisation for
    Economic Co-operation and Development Prospects
    for Hydrogen and Fuel Cells. 2005
  • Mawdsley J., Ferrandon M. Rossignol C., Ralph J.,
    Miller L., Kopasz J., Krause T. Catalyst for
    Autothermal Reforming FY 2003 Progress Report.
    Hydrogen, Fuel Cells and Infrastructure
    Technologies. Argonne National Laboratory.

26
References 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
    he/students/graduate/05_graduate_presentations/Roc
    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
    Grant Report Prepared for the California Energy
    Commission. May 2005
  • Sandia National Lab, United States Department of
    Energy. A. hydrogen Research
    Programhttp//www.ca.sandia.gov/hydrogen/index.ht
    mlB. Combustion Research Facilityhttp//www.ca.
    sandia.gov/crf/research/combustionEngines/PFI.php
  • Swain, M.R. Fuel Leak Simulation. University
    of Miami. Presented atProceedings of the 2001
    DOE hydrogen Program Review, 2001.
    http//www1.eere.energy.gov/hydrogenandfuelcells/p
    dfs/30535be.pdf
  • Turner J. Sustainable Hydrogen Production
    Science 13 August 2004 Vol. 305. no. 5686, pp.
    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/

27
References Contd
  • www.linde-gas.com/International/Web/LG/COM/likelgc
    om30.nsf/DocByAlias/ind_pox
  • http//www.getenergysmart.org/Files/HydrogenEducat
    ion/8HydrogenProductionCoal.pdf
  • www.getenergysmart.org/Files/HydrogenEducation/6Hy
    drogenProductionSteamMethaneReforming.pdf
  • http//www.getenergysmart.org/Files/HydrogenEducat
    ion/5HydrogenProductionOverview.pdf
  • http//www.getenergysmart.org/Files/HydrogenEducat
    ion/7HydrogenProductionNuclear.pdf
  • www.whitehouse.gov/news/releases/2006/01/20060131-
    6.html
  • http//archives.cnn.com/2001/TECH/science/03/16/hy
    drogen.cars/
  • http//www.fossil.energy.gov/programs/powersystems
    /gasification/howgasificationworks.html
  • http//www.ca.sandia.gov/hydrogen/research/product
    ion/electrolysis.html
  • http//www.chewonkih2.org/docs/PEM20vs20Alkaline
    .pdf
  • http//www.princeton.edu/benziger/PEMFC.pdf
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