Q.1: Chlorobenzene (C&HSCI), an important solvent, is produced by bubbling chlorine gas through liquid benzene (C&Hs) in the presence of catalyst. In an undesired side reaction, the product is further chlorinated to dichlorobenzene, and in a third reaction the dichlorobenzene is chlorinated to trichlorobenzene. The reactions involved in the process are: C,H6 + Cl2 → CgH;Cl + HCl C,H5CI + Cl2 → C,H4CI2 + HCI C,H,Cl2 + Cl2 → C,H3CI3 + HCI The feed to the reactor consists of pure benzene and a technical grade of chlorine aas (98 wt% C2, the balance gaseous impurities with an average

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Q.1: Chlorobenzene (C6HSCI), an important solvent, is produced by bubbling
chlorine gas through liquid benzene (C6H6) in the presence of catalyst. In an
undesired side reaction, the product is further chlorinated to dichlorobenzene,
and in a third reaction the dichlorobenzene is chlorinated to trichlorobenzene.
The reactions involved in the process are:
C,H6 + Cl2 → C,H5CI + HCl
C6H5CI + Cl2 → C,H4CI2 + HCl
C,H,Cl2 + Cl2 → C6H3C!3 + HCl
The feed to the reactor consists of pure benzene and a technical grade of
chlorine gas (98 wt% Cl2, the balance gaseous impurities with an average
molecular weight of 25.0). The liquid output from the reactor contains 73.2
mol% C6H6, 25.0 mol% CóH5CI, 1.5 mol% CóHĄC2, 0.3 mol% CsH3Cl3. The gaseous
output contains only HCI and the impurities that entered with the chlorine. With
100 mol of liquid output,
a) Using extent of reaction method, calculate the following:
1. The percentage by which benzene is fed in excess.
2. The fractional conversion of benzene.
3. The fractional yield of chlorobenzene.
b) For the feed, why is pure chlorine not used instead of the chlorine gas
with impurities?
Transcribed Image Text:Q.1: Chlorobenzene (C6HSCI), an important solvent, is produced by bubbling chlorine gas through liquid benzene (C6H6) in the presence of catalyst. In an undesired side reaction, the product is further chlorinated to dichlorobenzene, and in a third reaction the dichlorobenzene is chlorinated to trichlorobenzene. The reactions involved in the process are: C,H6 + Cl2 → C,H5CI + HCl C6H5CI + Cl2 → C,H4CI2 + HCl C,H,Cl2 + Cl2 → C6H3C!3 + HCl The feed to the reactor consists of pure benzene and a technical grade of chlorine gas (98 wt% Cl2, the balance gaseous impurities with an average molecular weight of 25.0). The liquid output from the reactor contains 73.2 mol% C6H6, 25.0 mol% CóH5CI, 1.5 mol% CóHĄC2, 0.3 mol% CsH3Cl3. The gaseous output contains only HCI and the impurities that entered with the chlorine. With 100 mol of liquid output, a) Using extent of reaction method, calculate the following: 1. The percentage by which benzene is fed in excess. 2. The fractional conversion of benzene. 3. The fractional yield of chlorobenzene. b) For the feed, why is pure chlorine not used instead of the chlorine gas with impurities?
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