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Modern Engineering Thermodynamics

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15.15 Fuel Cells 639<br />

The maximum power _W max and maximum reaction efficiency ðη r Þ max<br />

occur when the device is completely reversible<br />

or _S P = 0: Then,<br />

ðη r Þ max =<br />

∑<br />

in<br />

∑<br />

in<br />

_m i g i −∑<br />

out<br />

_m i h i −∑<br />

out<br />

_m i g i<br />

_m i h i<br />

=<br />

∑<br />

in<br />

∑<br />

in<br />

_n i g i −∑ _n i g i<br />

out<br />

(15.42)<br />

_n i h i −∑ _n i h i<br />

out<br />

Utilizing Eq. (15.33), the molar forms of Eqs. (15.40), (15.41), and (15.42) are<br />

_W = ∑<br />

R<br />

_n i g • i<br />

−∑<br />

P<br />

<br />

_n i g • i<br />

− T b<br />

_S P + RT ln ∏<br />

R<br />

ðp i /p° Þ _ni /∏ ðp i /p°<br />

P<br />

Þ _ni<br />

<br />

(15.43)<br />

and<br />

η r =<br />

∑<br />

R<br />

_n i g • i −∑<br />

P<br />

_n i g • i − T b<br />

_S P + RT ln ∏<br />

R<br />

∑<br />

R<br />

_n i h i −∑<br />

P<br />

ðp i /p° Þ _ni /∏ ðp i /p°<br />

P<br />

Þ _ni<br />

_n i h i<br />

(15.44)<br />

ðη r Þ maximum<br />

fuel cell<br />

efficiency<br />

=<br />

∑<br />

R<br />

ðn i /n fuel<br />

Þg • i<br />

−∑<br />

P<br />

ðn i /n fuel<br />

∑<br />

R<br />

Þg • i<br />

+ RT ln ∏<br />

R<br />

ðn i /n fuel<br />

Þh i −∑<br />

P<br />

ðp i /p°<br />

ð<br />

Þ ni/n fuel Þ /∏<br />

P<br />

ðp i /p°<br />

ð<br />

Þ ni/n fuelÞ <br />

ðn i /n fuel Þh i<br />

(15.45)<br />

If the reactants or products are unmixed and the pressure of each species (or component) in the reaction is<br />

0.1 MPa, then p i = p° and ∏ P<br />

ðp i /p° Þ ni = ∏ R<br />

ðp i /p° Þ ni = 1:0 in these three equations. Otherwise, if the reactants are<br />

premixed or the product gases are mixed (as they normally are) at a total pressure p m , then the partial pressure of<br />

each component gas must be determined. Further, if all the gases present are ideal gases that obey the Gibbs-<br />

Dalton ideal gas mixture law, then the partial pressures can be expressed in terms of the mole fractions as<br />

p i /p° = ðχ i p m Þ/p°, where x i is the mole fraction of gas i and p°=0.1 MPa. Then,<br />

h i<br />

ln ∏ðp i /p° Þ ni = ln ∏ðχ i p m /p° Þ ni<br />

in Eqs. (15.43), (15.44), and (15.45).<br />

In the case of a fuel cell, the output power appears as an electrical current I flowing through a potential<br />

(voltage) difference ϕ, and using Ohm’s law we can calculate the actual power output of the cell as<br />

_W = ϕI = I 2 R e<br />

where ϕ is the cell voltage, I is its current flow, and R e is the external resistance (recall that work output must be<br />

positive with our sign convention). Combining this equation with Eq. (15.40) gives the entropy production rate<br />

of the fuel cell as<br />

ð _S P Þ fuel<br />

cell<br />

= ∑<br />

P<br />

_n i g i −∑<br />

R<br />

Also, it can be shown that the electrical current I produced by a fuel cell is given by<br />

I = ð_n fuel ÞjF<br />

!<br />

_n i g + ϕI /T b ≥ 0 (15.46)<br />

where I is in amperes when _n fuel is in kgmole/s. In this equation j is the total valence of the fuel ions in kgmole<br />

of electrons per kgmole of fuel, and F is Faraday’s constant, defined as<br />

F = ð6:023 × 10 26 electrons/kgmole electronsÞð1:602 × 10 −19 coulombs/electronÞ<br />

= 96:487 kilocoulombs/kgmole electrons<br />

but since 1 coulomb = 1 joule/volt = 1 J/V, this can be written as<br />

F = 96,487 kJ/ðV . kgmole electronsÞ

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