The variants of condensation of vapor-gas mixtures formed during the dealkylation
of aromatic hydrocarbons are considered. A comparison of the operating options of the equipment
showed that the most profitable in the conditions of industrial use will be the use of a bypass water
condenser.
The main industrial methods of benzene production are considered. Comparison of the parameters of operation and purity of the obtained benzene of the main industrial hydrodealkylation plants showed the advantages of the catalytic process
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