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AssigneePhillips Petroleum Company
InventorsCharles A. Drake, An-Hsiang Wu
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A catalyst composition, a process for producing the composition, and a hydrotreating process for converting a hydrocarbon stream such as, for example, gasoline, to olefins and C.sub.6 to C.sub.8 aromatic hydrocarbons such as toluene and xylenes are disclosed. The catalyst composition comprises a zeolite, a clay, and a promoter. The process for producing the composition comprises the steps: (1) combining a zeolite with a clay and a promoter under a condition sufficient to bind the clay to the zeolite to produce a clay-bound zeolite; and (2) heating the clay-bound zeolite to produce a modified zeolite. The hydrotreating process comprises contacting a hydrocarbon stream with the catalyst composition under a condition sufficient to effect the conversion of a hydrocarbon to an olefin and a C.sub.6 to C.sub.8 aromatic hydrocarbon.
A composition comprising a ZSM-5 zeolite, a clay, and a promoter which comprises a mixture of zinc titanate and magnesium silicate or a mixture of zinc silicate and triethyl phosphate wherein the weight ratio of said promoter to said zeolite is in the range of from about 0.1:1 to about 0.5:1.
A composition comprising a ZSM-5 zeolite, a clay, and a promoter which comprises a mixture of zinc titanate and magnesium silicate or a mixture of zinc silicate and triethyl phosphate wherein the weight ratio of clay to zeolite is in the range of from about 1:20 to about 20:1 and wherein the weight ratio of promoter to zeolite is in the range of from about 0.1:1 to about 0.5:1.
A composition comprising ZSM-5 zeolite, bentonite, and a promoter which comprises a mixture of zinc titanate and magnesium silicate or a mixture of zinc silicate and triethyl phosphate wherein the weight ratio of bentonite to zeolite is in the range of from about 1:7 to about 5:1 and the weight ratio of promoter to zeolite is in the range of from about 0.1:1 to about 0.5:1.
Dependencies are inferred from the claim text.