FIELD: chemistry.
SUBSTANCE: invention relates to a process for producing paraxylene from a C4 stream and a C5+ catalytic naphtha stream from the catalytic cracking apparatus. Method comprises: a) separating a stream of C5-C9 non-aromatic compounds and a first stream of C6-C10 aromatic compounds from the C5+ catalytic naphtha stream, wherein step a) comprises a distillation step and an extraction step; b) forming a second stream of C6-C10 aromatic compounds from a C4 stream and a stream of C5-C9 non-aromatic compounds, wherein at least one of the C4 stream and stream of C5-C9 non-aromatic compounds contains olefins; c) removing impurities, via the impurity removal section, from the first and second C6-C10 aromatic streams to obtain a purified stream of C6-C10 aromatic compounds; d) directing catalytic reforming and pyrolysis products to the separation section; e) separating, in the separation section, the C6-C7 stream, the first C8 stream, the C9-C10 stream and the C11+ stream from purified streams of C6-C10 aromatic compounds and catalytic reforming and pyrolysis products; f) feeding the C6-C7 stream and the C9-C10 stream to the xylene production section to produce a second C8 stream; and g) feeding the first and second C8 streams to the paraxylene production section to produce high purity paraxylene, wherein the paraxylene production section comprises a paraxylene separation zone and a xylene isomerisation zone. Separation section comprises a distillation zone that includes a benzene column and a toluene column, and wherein the xylene generation section of step f) shares the benzene column and the toluene column of the separation section.
EFFECT: proposed method allows the use of light and heavy hydrocarbons.
8 cl, 2 dwg
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Authors
Dates
2018-08-20—Published
2013-03-14—Filed