Start-up process for improved selectivity in toluene disproporti

Chemistry of hydrocarbon compounds – Aromatic compound synthesis – By alkyl or aryl transfer between molecules – e.g.,...

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C07C 362

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active

053877322

ABSTRACT:
A process is provided for the disproportionation of a toluene feed stock that includes using an unconventionally low hydrogen to toluene mole ratio during reaction start-up, i.e., until the production of non-aromatics begins to stabilize; thereafter the ratio is increased. Reducing the hydrogen content at the beginning of the reaction substantially lessens any hydrogenation activity, thereby gaining optimum selectivities to benzene at a much sooner rate than that achieved using more conventional hydrogen to toluene ratios. The post start-up increase in hydrogen concentration following stabilized production of non-aromatics is generally believed to enhance the aging character of the catalyst, thereby preserving catalyst life. In practicing the invention, a reaction zone is established loading a metal-modified mordenite catalyst into the reaction zone. A toluene containing feed stock is continuously supplied to the reaction zone. Contemporaneous with the introduction of the toluene, hydrogen gas is introduced into the reaction zone to provide a hydrogen to toluene mole ratio of between 0.5 and 1.5. The feed stock contacts the catalyst forming a disproportionation product containing benzene, xylene(s) and non-aromatic by-products. The disproportionation product is continuously withdrawn and measured to determine its non-aromatic content. When the non-aromatic content of the disproportionation product stabilizes, the amount of hydrogen supplied to the reaction zone is increased.

REFERENCES:
patent: 3667973 (1972-07-01), Mitshe et al.
patent: 3780122 (1973-12-01), Pollitzer et al.
patent: 4665258 (1987-05-01), Butler et al.

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