Hydrocarbon conversion process employing essentially alumina-fre

Mineral oils: processes and products – Chemical conversion of hydrocarbons – Plural serial stages of chemical conversion

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208 61, 208 66, 208109, 208118, C10G 4716, C10G 6904, C10G 6912, C10G 1105

Patent

active

043702198

ABSTRACT:
A process for converting a hydrocarbonaceous feedstock in which a catalytically hydroprocessed or a catalytically reformed feedstock is contacted under cracking conditions with an essentially alumina-free intermediate pore size zeolitic catalyst and immediately thereafter with a second essentially alumina-free intermediate pore size zeolitic catalyst under cracking conditions less severe than the first contacting conditions. The less severe conditions in the second contacting stage are preferably obtained by employing a lower temperature, although use of a less active catalyst to attain this end is a possibility. A crystalline chromia silicate having a mole ratio of oxides SiO.sub.2 :Cr.sub.2 O.sub.3 of greater than about 20 to 1 and an intermediate pore size crystalline silicate of the ZSM-5 type having a mole ratio of oxides SiO.sub.2 :Al.sub.2 O.sub.3 of greater than about 200 are the preferred catalysts.

REFERENCES:
patent: Re29948 (1979-03-01), Dwyer et al.
patent: 4093560 (1978-06-01), Kerr et al.
patent: 4244807 (1981-01-01), Dautzenberg et al.
patent: 4309275 (1982-01-01), Mulaskey

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