| Hydrogen/Oxygen
Fuel Cell reactions: The negative electrode reaction: H2 ---> 2 H+ + 2 e- (V = 0.00 volts) The positive electrode reaction: O2 + 4 H+ + 4 e- ---> 2 H2O (V = -1.23 volts) |
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Fuel Cells in Transportation:
1.) Pollutants:
Operation
of a hydrogen fuel cell would emit only water and no local
pollutants.
Fuel cells can use other fuels such as methanol or hydrocarbons
such
as methane or even gasoline. Such a fuel cell requires a reformer
that extracts gaseous hydrogen from these fuels. A vehicle powered by
such
a fuel cell would emit only about 1% of the local pollutants emitted by
an ICE.
2.) Reformation: Fuel
cells used for transportation are able to use the thermochemical
gasification
of biomass resources such as agricultural residues. Methane can
also
be reformed into hydrogen using:
CH4 + 2 H2O
---> CO2 + 8 H+
+ 8e-
at the anode and
8e- +
8H+ + 2O2 ---> 4H2O
at the cathode
Also, kerosene, hydrazine, and formaldehyde can
be used as a primary fuel.
Fuel Cell Types:
Fuel Cells are best distinguished by their electrolyte:
1.) Proton Exchange
Membrane
Fuel Cells (PEM) use H+ ions to carry the charge. [60-120
0C]
2.) Phosphoric acid fuel
cells (PAFC) also use H+ ions. [160 - 220 0C]
3.) Solid oxide ceramic
fuel cells (SOFC) use O-- ions to carry charge. [900 -
1000
0C]
4.) Alkaline fuel cells
use OH- ions to carry charge. [60 - 120 0C]
5.) Molten-carbonate fuel
cells (MCFC) use CO3-- ions to carry charge.
[600 - 650 0C]
Comparison
of Various Types of Fuel Cells4
Advantages:
|
Phosphoric Acid FC |
Molten Carbon FC |
Solid Oxide FC |
Proton Ex. Memb. FC |
|
PAFC |
MCFC |
SOFC |
PEMFC |
|
H+ exchanged |
CO3-- exchanged |
O-- exchanged |
H+ exchanged |
|
250 mA/cm2 |
160 mA/cm2 |
?? mA/cm2 |
1000 mA/cm2 |
|
200oC |
600oC |
1000oC |
100oC |
|
Tolerant to CO2 |
No precious metal required |
No precious metal required |
Tolerant to CO2 |
|
Most advanced |
CO is a usable fuel |
CO is a usable fuel |
Low working temp. |
|
Applicable to small capacity
plants and vehicular uses |
Internal reforming in cells is feasible |
Internal reforming cells in cells is feasible |
Very high current density is
achievable |
|
|
High grade heat is available |
CO2 recycling is not required |
|
4
Anahara,
R.,
Disadvantages:
|
Catalyst needs precious metals
($$) |
Material problem related to cell life and
mechanical stability |
High T presents severe
constraints on cell materials |
CO content in fuel is strictly
prohibited and catalyst ($$) |
|
Pt catalyst is deactivated by CO |
CO2 source needed for cathode |
Relatively high electrolyte resistivity |
Water management in cell is difficult |
|
Low conductivity electrolyte management |
Phase change of electrolyte at high T |
|
Only low grade heat is available |
Ben's Fuel Cell Diagrams:
http://physics.indiana.edu/~brabson/p310/FC1.tif,
http://physics.indiana.edu/~brabson/p310/FC2.tif
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