The reaction occuring is
Formic acid is fed at 25°C and 1 atm
At T = 25°C formic acid is liquid
V = 100 L/min = 0.1 m3/min
T = 25°C = 298 K
Density of formic acid at T = 25°C = 1220 Kg/m3
Formic acid at inlet = (0.1) (1220) = 122 Kg/min
M. W of formic acid = 46 Kg/kmol
Moles of formic acid = 122/46 =
2.65217 kmol/min
formic acid is in outlet so all formic acid reacts
Air supllied is 100% excess
Oxygen required according to stiochiometry = (2.65217) (0.5) = 1.326085 moles
But o2 supplied = 1.326085(2) = 2.65217 mol/min
Air supplied = 2.65217/(0.21) =
12.6293 kgmol/min
The products leave at 70°C
Cp of products is taken at average temperature of (25+70) /2 = 47.5°C = 320.65 K
Reference enthaply is at T= 25°C
So ∆H(reactants) = 0
Product analysis
Component | kmol/min | Cp(KJ/mol°C) | H(KJ/min) |
CO2 | 2.65217 | 38.070 | 4543.565 |
H2O | 2.65217 | 33.693 | 4021.18 |
O2 | 1.326085 | 29.536 | 762.52 |
N2 | 12.6293(0.79) = 9.9772 | 29.146 | 13085.796 |
Total | 25.6029 | 22413.061 |
H(products) = 22413.061 KJ/min
From handbook at T = 25°C
∆Hf(CO2) (g) = -393. 5 KJ/mol
∆Hf(H2O) (g) = -241. 83 KJ/mol
∆Hf(HCOOH) (L) = -425. 5 KJ/mol
∆Hr = ∆Hproducts - ∆Hreactants
∆Hr = (-241.83) +(-393.5) -(-425.5) =
-209. 83 KJ/mol
Moles of formic acid reacted =2.65217 kmol/min
∆Hr = -209. 83(1000) (2.65217) =
-556504. 8311 KJ/min
Total energy
Q = ∆Hr + H(products)
Q = -556504. 8311 + 22413.061
Q = -534091. 7701 KJ/min = -8901. 529 KW
Fuel cell transfers to the surroundings 1.50(1000) KW of heat = 1500 KW
Doing energy balance electrical energy produced = 8901.529 - 1500 = 7401.529 KW
Electrical power = 7401.529 KW
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