Method of dehydrogenation of alkyl aromatics to alkenyl aromatics
AssigneeThe Dow Chemical Company
InventorGeorge W. Lyon
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AssigneeThe Dow Chemical Company
InventorGeorge W. Lyon
Estimating the term…
A method for dehydrogenating an alkyl aromatic compound, particularly, ethylbenzene or ethyl toluene, to its corresponding vinyl aromatic derivative, styrene or methyl styrene, respectively, in which the alkyl aromatic compound and its normally attendant diluent, stream or water, are preheated to a temperature below which any substantial thermal reaction temperature of the alkyl aromatic compound occurs, viz., 450.degree. to about 500.degree. C., and introduced into a catalytic bed of a reactor and thereafter contacted and mixed in said catalytic bed with a quantity of steam in an amount and at a temperature to raise the alkyl aromatic compound to the catalytic dehydrogenation temperature. The steam introduced into the catalyst bed, in a ratio less than 3 to 1 to about 0.7 to 1, steam to hydrocarbon passes through the bed in heat exchange relationship to the catalyst and the reacting gases prior to contacting and mixing with the alkyl aromatic compound in the bed.
A method for dehydrogenating an alkylbenzene compound having from 1 to 3 alkyl groups attached to a benzene nucleus of which 1 to 2 alkyl groups contain 2-3 C atoms comprising feeding said alkylbenzene compound at a temperature of 450.degree.-500.degree. C. through the inlet port of a reactor, feeding stream at a temperature of 650.degree. to about 1000.degree. C. into the interior of a fixed bed of dehydrogenation catalyst, said stream flowing in a countercurrent manner to said flow of alkylbenzenes in heat exchange relationship in said bed prior to introduction into said bed, said point of introduction being just below the point of introduction of the alkylbenzene compound into said bed, said steam being supplied in sufficient quantity to maintain the mixture, at a temperature of about 575.degree. to 675.degree. C. upon mixing the alkybenzene and steam in said catalyst bed, passing the mixture through said catalyst bed and withdrawing reacted effluent from the reactor, the total steam to hydrocarbon ratio weight to weight basis, being less than about 3 to 1, to about 0.7 to 1 each respectively.
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