A mixture of benzene gas with 60 % excess air contained in a constant-volume tank undergoes the combustion. Determine the net heat transfer. Product-temperature is 1,000 K. Use the data given below:
h1000K kJ/ kmol |
h298K kJ/ kmol |
hf0 kJ/ kmol |
Substance |
– – – | – – – | 82,930 | C6H6(g) |
31,389 | 8682 | 0 | O2 |
30,129 | 8669 | 0 | N2 |
35,882 | 9904 | -241,820 | H2O(g) |
30,355 | 8669 | -110,530 | CO |
42,769 | 9364 | -393,520 | CO2 |
Given: (1) Combustion reactants: Air and benzene, (2) Excess air: 60%
Find out: heat transferred per kmol of benzene.
Properties: Molar mass of C, H2 and O2 and air are: 12 kg/kmol, 2 kg/kmol, 32 kg/kmol and 29 kg/kmol
respectively.
Assumption: (1) Combustion is complete, (2) Air and combustion gases are ideal (3) Kinetic and potential energies are negligible (4) Combustion products are H2O, CO2 and N2 only.
Combustion reaction with no-excess air will be:
C6H6+(7.5 O2+28.2 N2)⟶6 CO2 + 3 H2O(28.2 N2)
From the first law:
For constant volume,
Q–W=∑NR(Hf0+H–H0–pV)R–∑NP(Hf0+H–H0–pV)p
With W = 0,
Q=∑NR(Hf0+H–H0–pV)R–∑NP(Hf0+H–H0–pV)p
Assuming ideal gas condition:
Q=∑NR(Hf0+H–H0–RT)R–∑NP(Hf0+H–H0–RT)p
From the given table data:
∑NP(Hf0+H–H0–RT)p=6×(−3,93,520+42,769–9,364–8.314×1,000)+3×(−2,41,820+35,882–9,904–8.314×1,000)+28.2×(0+30,159–8,669–8.314×1,000)
= –24,81,766 kJ/kmol
∑NR(Hf0+H–H0–RT)R=1×(82,930−8.314×1,000)+7.5×(−8.314×1,000)+28.2×(−8.314×1,000)
= –7,996.89 kJ/kmol.
So, Q = –24,81,766 – (–7,996.89) = –24,73,769.11 kJ/kmol.
Negative sign indicates heat outgoing.