Title: Eng/Phy 160, May 25,05
1Eng/Phy 160, May 25,05
- The Hydrogen Economy
- Overview an alternative to the oil economy for
transportation especially - Hydrogen energy storage (as fuel), not energy
source. Means of production (electrolysis,
nuclear, fossil fuel, bio) basic reaction - Means to Utilize Internal combustion vs. fuel
cell kinds of fuel cells technological needs - Hydrogen Storage Overview of current technology
and goals - Hydrogen Infrastructure What is necessary for
conversion costs, opportunities - Downsides Safety and Environmental risks
2Paper II due by email by day of final
- The use of coal for generating transportation
fuel has been in the news recently due to
politicians from both parties - Bush administration FutureGenproject (to generate
electricity and hydrogen fuel from coal)
http//www.fossil.energy.gov/programs/powersystems
/futuregen/ - Gov. Brian Schweitzer of Montanas plans for
sythetic fuel from coal http//governor.mt.gov/ho
ttopics/faqsynthetic.asp and http//sexton.ucdavis
.edu/CondMatt/cox/03schweitzer.html - Your job is the following Choose one or the
other of the coal plans (from Pres. Bush or Gov.
Schweitzer) and analyze it to assess (i) will it
provide ample fuel from coal at a reasonable cost
over an extended time frame, (ii) do the benefits
offset costs (here you must assess the
environmental damage from coal mining and carbon
dioxide production). Then come to a reasoned
argument for or against the plan, and write an
essay in the form of a letter to the President or
Governor expressing your support or opposition.
Your letter is limited to two pages. It must
include (1) the correct address of the President
or Governor in the header, (2) Your correct
address and contact information (if you are
nervous about privacy here make these up). (3)
References on an accompanying page to support
your arguments. Here you can rely upon Modern
Language Association formats (see
http//www.lib.ucdavis.edu/dept/hss/mla.php).Your
paper must be typed. - Papers will be graded on a 10 point scale, and I
will be looking most importantly for quality
reasoning, good writing mechanics (sentence
construction, paragraph construction, spelling
and grammar), and good sources.
3The Hydrogen Economy a vision of a different
transporation system
- Utilize hydrogen as a fuel rather than oil
derived products. - Can convert to more efficient energy systems
- Can employ hydrogen derived from existing fossil
fuels in the interim on the way to sustainable
hydrogen production. - Hydrogen can also be used in other applications
(stationary source power generation for industry,
e.g.)
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6Hydrogen fundamentals
- Hydrogen is a storage form there is not free
hydrogen sitting around for us to access as there
is fossil fuel. The basic oxidation reaction
(burning) of Hydrogen goes as - 2H2 O2 ? 2H2O 132 MJ/kg-H2
- Some contrast Best fuel per mass (problem is low
density)
Fuel Oxidation Energy release (MJ/kg)
Hydrogen 120
Gasoline 47
Natural Gas 36-42
Coal 30
Wood 21
Manure 13
7Hydrogen Fundamentals Cont.
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?
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8How to get hydrogen?
- Renewable Employ electrolysis/high T run
combustion reaction in reverse - 132 MJ/kg-water H2O ? H2 ½ O2
- Electrolysis Use wind, solar, or nuclear to
provide spark for hydrogen - Catalytic at high temperature Create good
catalytic chemistry in water of nuclear plant to
generate and hydrogen (remember in Chernobyl and
TMI hydrogen was a factor!)
9Hydrogen from fossil fuels
- Reforming
- Example of Methane
- CH4 ½ O2 ? CO 2H2
- CO H2O ? CO2 H2
- CH4 ½ O2 H2O ? CO2 3H2___
- Generally, it is possible to have less CO2 per
reformed hydrogen produced than per fossil fuel
burned (meaning of table 13.1 in Deutsch and
Lester) - Comparison Assume 80 conversion efficiency of
methane in reformer to hydrogen at ideal
conversion, there will be about 0.33 moles of
carbon dioxide produced per mole of hydrogen
according to the above. At 80 conversion
efficiency, there will be some straight oxidation
of methane and hence 0.33/0.8 0.41 moles of CO2
per mole of hydrogen. The number of moles from
straight burning of methane would be 1. - Can also get from steam reforming of coal (as in
futuregen) - Message need to consider well to wheel
efficiency
10Methane Splitting
- Demonstrated in 1970s by Norman Thagard.
- Large Heat Input
- 1600-2000 C
- Solution Solar Power
- (focus heat to split methane)
- 50 of Arizona to meet
- U.S. energy needs.
- Process still being developed.
11Aerosol Flow Reactor
- Energy produced at 13/GJ
- Half the energy requirements of
- Steam Methane Reforming
- Carbon Product Can Be Sold for ca. .66/kg
(market may get flooded with cheap carbon) - Reduce CO2 emissions by replacing current carbon
production industry - Dependent upon methane supply
12Biogeneration of hydrogen
13Implementation Fuel Cells vs. Internal
Combustion
- Fuel Cell Generate electricity by the
burning of hydrogen in a chemical cell
-
- Anode side 2H2 gt 4H 4e-
- Cathode side O2 4H 4e- gt 2H2O
- Net reaction 2H2 O2 gt 2H2O
14Overview from BES Report (great job!) (available
on class web site)
- Fuel H2 (produced from fossil fuel reformer,
electrolysis, nuclear plants, or biological
sources) or light molecule (e.g., methanol). - Low Temperature Fuel Cell Membrane hydrated
polymer electrolyte material Cathode
nanoparticle Pt on support Anode for pure H2,
Pt again for reformed H2 or methanol, PtRu
alloy. - High Temperature Fuel Cell Membrane oxygen
deficient metal oxide Electrodes conducting
(La,Sr)MnO3
15Proton Membrane
- The anode conducts the electrons that are freed
from the hydrogen molecules. It disperse the
hydrogen gas equally over the surface of the
catalyst. - The cathode, the positive post of the fuel cell,
distributes the oxygen to the surface of the
catalyst. It also conducts the electrons back
from the external circuit to the catalyst, where
they can recombine with the hydrogen ions and
oxygen to form water. - The electrolyte is the proton exchange membrane.
This specially treated material, which looks
something like ordinary kitchen plastic wrap,
only conducts positively charged ions. The
membrane blocks electrons. - The catalyst is a special material that
facilitates the reaction of oxygen and hydrogen.
It is usually made of platinum powder very thinly
coated onto carbon paper or cloth. The catalyst
is rough and porous so that the maximum surface
area of the platinum can be exposed to the
hydrogen or oxygen. The platinum-coated side of
the catalyst faces the PEM.
16Advantages of PEMFC
- PEMFCs operate at a fairly low temperature (about
176 degrees Fahrenheit, 80 degrees Celsius),
which means they warm up quickly and don't
require expensive containment structures.
Constant improvements in the engineering and
materials used in these cells have increased the
power density to a level where a device about the
size of a small piece of luggage can power a car.
17Some issuesplatinum in electrodes
- There is at present abundant platinum
- But platinum is not cheap! (47K/kg)
- Pure platinum at anodes gets poisoned
(adsorbed species limit catalysis)- must alloy
with e.g., Ru (also lowers cost)
18ObstaclesOpportunities for Research!
- Membrane Greater stability less corrosion
maintain hydration while running at higher
temperatures to improve heat rejection higher
ion mobility. - Cathode Replace or reduce Pt (, scarcity for
large scale production!) reduce overpotential
lower corrosion. - Anode Replace or reduce Pt avoid poisoning in
reformer or methanol based systems avoid
impurity increase of overload. - Overall Reduce amount of water in cell.
19Overpotential
Overpotential Difference between Ideal and
actual Potential in open circuit
Illustration of overpotential concept for
hydrogen fuel cell (from http//faculty.washington
.edu/stuve/chula03/ ecat_chula_lec5-4.pdf) (NB
anode overpotential can be increased with
contamination from reformed H2 or methanol)
20Better electrodes through combinatorial
chemistry?(P. Strasser et al., High throughput
experimental and theoretical predictive screening
of materials-a comparative study of search
strategies for new fuel cell anode catalysts,
J. Phys. Chem. B 107, 11013 (2003).
21Promise of nanoscience?
- Novel Catalysts at nanoscale? It is possible that
Pt may be replaced by some materials may become
catalytic at nanoscale (eg, Au) or have dramatic
increased catalytic activity due to, e.g., novel
structures or surface layers (MgO-catalytic
degradation of organochloranes I.V. Mishakov et
al., Nanocrystalline MgO as a
dehydrohalogenation catalyst, Journal of
Catalysis 286, 40 (2002). BUT This seems much
harder and in search of a silver bullet. - Novel Catalytic Supports at the nanolayer By
improving catalytic supports to better orient and
align Pt nanoparticles, you might reduce Pt usage
through better structuring (e.g., S. Han, Y. Yun,
K.W. Park, Y.E. Sung, T. Hyeon, Simple
Solid-phase synthesis of hollow graphitic
nanoparticles and their application to direct
methanol fuel cells, Advanced Materials 15,
1922 (2003).)
22Opportunities from Biology?
- Numerous proteins reduce oxygen--use at cathode?
Cytochrome C oxidase (key respiration protein!)
overall reaction same as fuel cell! (4e-4HO2
-gt 2H20) Laccase oxidizes phenols and alanines
while reducing oxygen. (In all cases, oxygen
docks at transition metal site or complex)
Structure of cytochrome C oxidase (metalloprotein
data base- http//metallo. scripps.edu/ PROMISE/ 1
OCC.html
Structure of a fungal laccase protein-three
copper sites in yellow
http//akseli.tekes.fi/Resource.phx/bike/rakbio/en
/rouvinenkoivula.htx
23A WORKING BIOFUELCELL! (E. Katz and I.
Willner, A biofuel cell with electrochemically
switchable and tunable output, J. Am. Chem.
Soc. 125, 6803 (2003))
Apparatus schematicjust add sugar!
Cathode schematic (cyt C cyt C oxidase)
tunable!!
Anode schematic (APO glucose oxidase)
24ICE
- Take advantage of the existing massive ICE
framework - Disadvantage much lower well-to-wheels
efficiency due to low efficiency of IC engine.
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26Storage
27Some compounds being researched
28Delivery Options for H economy
- Gaseous
- Pipelines
- Trucks
- On-site reforming
- Liquid H2 Chemical carriers
- Trucks, Rails (liquid H2)
- Hydrides (solid carriers)
- Other carriers (barges, etc)
29Barriers
- Lack of infrastructure options analysis
- High capital cost of pipelines
- High cost of compression
- High cost of liquefaction
- Lack of cost effective carrier technology
- Hydrogen infrastructure exists only for small
merchant hydrogen markets in the chemical and
refining industries
30DOE Targets
31Estimates of Delivery Cost
- Accenture estimates a 280 billion U.S.
investment in hydrogen fueling infrastructure, - 130 B to convert fueling stations
- 70 B to for natural gas and ethanol supplies
- 40 B to move fuel to fueling stations
- 40 B for new pipelines
- But, keep in mind that by 2020 annual oil imports
will be 200 B
32Pipeline Transition Cost Reduction
- Estimated transition cost of 40 B.
- The technology already exists
- Currently, there are 1,500 km (930 miles) of
special hydrogen pipelines (720 km or 446 miles
in North America) operating at up to 100 bar. - Natural gas pipelines can be used or adapted for
delivery with acceptable energy loss - Future pipelines created for petroleum
transportation are hydrogen compatible - Japan intended major Siberia-China-Japan gas
pipeline
33Alternative to hydrogen - Methanol Fuel Cells
- Partial oxidation of methane
- CH4 ½ O2 ? CH3OH -- exothermic!
- Liquid at ambient conditions. Can be used in
fuel cells with the net reaction - CH3OH 3O2 ? 2H2O CO2 22 MJ/kg
- Note that
- The generation reaction can be used for
electricity say. - Given the enhanced fuel cell/electric motor
efficiency relative to straight burning of fossil
fuels, less CO2 is produced per burn by 2 x - Can plausibly be used for consumer electronics at
greater efficiency than recharging via
conventional electricity sources and hence less
CO2. - In principle, methane can be produced
biologically (eg, collecting from waste dumps or
cow burps) -