5 to about 70 kg cm 2 and a stoichiometric ratio of hydrogen to olefins from about 1 1 to about 5 1 olefin treated reformate is shown in a line 9 the reformate comprising aromatics non aromatics and light ends in a line 9 is combined with a transalkylation unit effluent in line 17 and an ethylbenzene dealkylation and isomerization unit effluent in a line 18 and sent to a transalkylation stripper fractionation zone 54 via a line 19 the transalkylation stripper fractionation zone 54 generally comprises at least one fractionation column the transalkylation stripper fractionation zone 54 produces a benzene and lighter fraction which contains benzene and lighter hydrocarbons including c 7 and lighter aliphatic hydrocarbons in a line 21 and a toluene and heavier fraction which contains toluene xylenes heavier aromatics and c 8 and heavier aliphatic hydrocarbons in a line 22 the toluene and heavier fraction is directed in line 22 to toluene column 31 toluene column 31 produces an overhead toluene enriched stream in a line 32 and the bottom of the toluene column 31 produces the xylene plus enriched stream in line 33 the toluene enriched stream in line 32 from the overhead of the toluene column 31 is sent to a transalkylation unit 36 described below of the aromatics complex the xylene plus enriched stream in line 33 from the bottom of the toluene column 31 is sent to a xylene recovery section 55 described below of the aromatics complex a.