Gasoline sulfur reduction in fluid catalytic cracking
AssigneeW. R. Grace & Co.-Conn.
InventorsArthur W. Chester, Terry G. Roberie, Hye Kyung C. Timken, Michael S. Ziebarth
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AssigneeW. R. Grace & Co.-Conn.
InventorsArthur W. Chester, Terry G. Roberie, Hye Kyung C. Timken, Michael S. Ziebarth
Estimating the term…
The sulfur content of liquid cracking products, especially the cracked gasoline, of the catalytic cracking process is reduced by the use of a sulfur reduction catalyst composition comprising a porous molecular sieve which contains a metal in an oxidation state above zero within the interior of the pore structure of the sieve as well as a cerium component which enhances the stability and sulfur reduction activity of the catalyst. The molecular sieve is normally a faujasite such as USY. The primary sulfur reduction component is normally a metal of Period 3 of the Periodic Table, preferably vanadium. The sulfur reduction catalyst may be used in the form of a separate particle additive or as a component of an integrated cracking/sulfur reduction catalyst.
A method of reducing the sulfur content of a catalytically cracked petroleum fraction which comprises catalytically cracking a distillate petroleum feed fraction containing substituted-benzothiophenes and dibenzothiophene organosulfur compounds under fluid catalytic cracking conditions at elevated temperature in the presence of a catalytic cracking catalyst and a product sulfur reduction catalyst, wherein the product sulfur reduction catalyst comprises a porous molecular sieve which contains (i) a first metal component comprising vanadium in an oxidation state greater than zero within the interior pore structure of the molecular sieve and (ii) a second metal component comprising cerium within the interior pore structure of the molecular sieve, to produce a liquid cracked distillate product fraction having a reduced content of substituted-benzothiophenes and dibenzothiophene organosulfur compounds.
In a fluid catalytic cracking process in which a heavy hydrocarbon feed comprising a distillate petroleum hydrocarbon fraction containing substituted-benzothiophenes and dibenzothiophene organosulfur compounds is catalytically cracked by contact in a cyclic catalyst recirculation cracking process with a circulating fluidizable catalytic cracking catalyst inventory consisting of particles having a size ranging from about 20 to about 100 microns, comprising:
Dependencies are inferred from the claim text.