In: Other
2. In manufacture of chlorine, feed containing hydrochloric acid
gas and air are fed to the reactor. The product gases leaving the
reactor are found to contain 13.2% HCl, 6.3% 02, 42.9% N2, 30% Cl2
and 7.6% H2O (by weight). Calculate:
i) The percent excess air used.
ii) The composition of gases entering reactor
iii) The degree of completion of oxidation (conversion)
(Hint: Start solving by change the mass flow rate to mol flow rate
first.)
The balanced reaction
4 HCl + (O2 + 3.76 N2) = 2 Cl2 + 2 H2O + 3.76 N2
Let the mass of product gas = 100 g
Moles of HCl = mass/molecular weight
= 13.2g / 36.5g/mol
= 0.3616 mol
Moles of O2 = 6.3g / 32g/mol = 0.1968 mol
Moles of N2 = 42.9/28 = 1.532 mol
Total Moles of air = moles of O2 + moles of N2
= 0.1968 + 1.532 = 1.7288 mol
Moles of Cl2 = 30/71 = 0.4225 mol
Moles of H2O = 7.6/18 = 0.4222 mol
At inlet
Moles of HCl converted
= 4 mol HCl x 0.4225 mol Cl2 produced / 2 mol Cl2
= 0.8450 mol
Total Moles of HCl = Moles of HCl converted + Moles of HCl at outlet
= 0.8450 + 0.3616
= 1.2066 mol
Stoichiometric Moles of O2
= 1 mol O2 x 0.8450 moles of HCl converted / 4 mol HCl
= 0.2113 mol
Stoichiometric air required = 0.2113/0.21 = 1.006 mol
Actual moles of O2 supplied = Stoichiometric Moles of O2 + Moles of O2 at outlet
= 0.2113 + 0.1968 = 0.4081 mol
Moles of N2 supplied = 1.532 mol
Actual Moles of air supplied = moles of O2 + moles of N2
= 0.4081 + 1.532
= 1.94 moles
Part a
% excess air used
= ( actual air - stoichiometric air) *100 / (stoichiometric air)
= (1.94 - 1.006)*100/(1.006)
= 92.84 %
Part b
Total gases entering = moles of HCl + moles of air
= 1.207 + 1.94
= 3.147 mol
Part c
Conversion = (HCl converted) *100 / (HCl supplied)
= (0.8450)*100/(1.2066)
= 70.06 %