Methanol is obtained from carbon monoxide and hydrogen, according to:
Suppose 100 m3/h of reagent mixture is fed in stoichiometric amounts, at 35°C and 1 atm. If 17.2 kW of heat is removed from the reactor, determine the conversion rate (using four decimal places) of the reaction when the outlet temperature is 135°C.
The reaction occurring is
Volumetric flowrate = 100 m3/h
T = 35°C = 308 K
P = 1 atm = 1.013×105 Pa
n = PV/(RT)
n = (1.013×105×100)/(8.314×308)
n = 3955.931 mol/h
Stiochiometric amount is supplied
Moles of CO = 3955.931(1/3)= 1318.643 mol/h
= 0.36628 mol/s
Moles of H2 = 2637.2873 mol/h = 0.73257 mol/s
At T = 25°C , from handbook
∆Hf(CO)(g)= -110.53 KJ/mol
∆Hf(CH3OH)(g)= -205 KJ/mol
∆Hf(H2)(g)= 0
∆Hr = ∆Hproducts - ∆Hreactants
∆Hr = -205 -(-110.53)
∆Hr (25°C)= -94.47 KJ/mol
From handbook at average temperature of (25+35)/2 = 30°C
Cp(CO)= 29.1545 J/mol K
Cp(Methanol)= 44.3938 J/mol K
Cp(H2)(g)= 28.859 J/mol K
∆Cp =(nCp) products -(nCp)reactants
∆Cp = (44.3938) -(2×28.859) - 29.1545= -42.478
Kirchoffs law
∆H(35°C) = ∆H(25°C)+ ∆Cp(35-25)
∆H(35°C)= -94.47(1000)+ (-42.478)(35-25)= -94.894 KJ/mol
Let x be amount of methanol reacted
Outlet temperature = 135°C
Enthaply reference = 25°C
Reactant average temperature = (35+25)/2 = 30°C
Product average temperature = (35+135)/2 = 85°C
All cp values are taken at average temperature from handbook
Component | inlet moles (mol/s) | Cp | Hi | outlet moles (mol/s) | Cp | Ho |
CO | 0.36628 | 0.0291545 | 0.1067 | 0.36628-x | 0.029237 | |
H2 | 0.73256 | 0.028859 | 0.2114 | 0.73256-(2x) | 0.029041 | |
Methanol | 0 | 0.0443938 | - | x | 0.048496 | |
Total | 0.3181 |
Q = ∆Hr(x)+ Ho + Hi
Q = 17.2 KW
- 17.2 = -94.894(x)+ 0.3181 +
((0.36628-x)(0.029237)+ (0.73256-2x)(0.029041)+ (0.048496(x))(135-35)
x = 0.209730 mol/s
Initial moles = 0.36628 mol/s
Conversion =
( (0.36628-0.209730)/(0.36628))(100) = 42.74052 %
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