FIELD: devices for hydrocarbon catalytic dehydrogenation; applicable in petrochemical industry for dehydrogenation of ethylenebenzene into styrene. SUBSTANCE: uniform distribution of flow in reactor is attained due to maintaining of portion of holes of internal and external coaxial perforated cylinders in ratio 0.68:1. In this case, distance between perforated cylinders equals 0.08 of perforated part height. Central body of revolution is described by formula given in the invention description. EFFECT: higher efficiency of process. 1 dwg
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Authors
Dates
2000-08-20—Published
1999-07-05—Filed