Process for reducing CO and SOx emissions from catalytic cracking units

Claim 2

In a cyclical catalytic cracking process wherein cracking catalyst particles are continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a sulfur-containing hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with catalyst particles circulating therethrough, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are then passed through said regeneration zone wherein said coke on said cracking catalyst particles is combusted, thereby reactivating the catalyst and producing a SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by introducing bastnaesite particles in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones, said bastnaesite particles being particles of natural bastnaesite or a treated natural bastnaesite containing at least some of its original flourine.

Claim 3

In a cyclical catalytic cracking process wherein cracking catalyst particles are continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a sulfur-containing hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with catalyst particles circulating therethrough, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are then passed through said regeneration zone wherein said coke on said cracking catalyst particles is combusted, thereby reactivating the catalyst and producing a SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by introducing particles of natural bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones.

Claim 4

In a cyclical catalytic cracking process wherein cracking catalyst particles are continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a sulfur-containing hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with catalyst particles circulating therethrough, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are then passed through said regeneration zone wherein said coke on said cracking catalyst particles is combusted, thereby reactivating the catalyst and producing a SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by introducing particles of natural bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones.

Claim 5

In a cyclical catalytic cracking process wherein cracking catalyst particles ae continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a sulfur-containing hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with catalyst particles circulating therethrough, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are then passed through said regeneration zone wherein said coke on said cracking catalyst particles is combusted, thereby reactivating the catalyst and producing a SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by more than 75% by introducing particles of natural bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones.

Claim 6

In a cyclical catalytic cracking process wherein cracking catalyst particles ae continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a sulfur-containing hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with catalyst particles circulating therethrough, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are then passed through said regeneration zone wherein said coke on said cracking catalyst particles is combusted, thereby reactivating the catalyst and producing a SO x -containing flue gas, and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of SO x compounds carried with said flue gas by more than 75% by introducing particles of natural bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones.

Claim 7

In a cyclic catalytic cracking process wherein cracking catalyst particles comprising a crystalline aluminosilicate zeolite are continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with said circulating catalyst particles under conditions sufficient to convert said feedstock to more valuable hydrocarbons of lower average molecular weight and lower average boiling point than said feedstock while said catalyst particles become deactivated with coke deposits, and said catalyst particles are then passed through a regeneration zone and reactivated by burning said coke off said catalyst particles under conditions whereby a flue gas containing carbon monoxide and carbon dioxide is produced, and said catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the rate at which carbon monoxide in said flue gas is discharged from said regeneration zone on a mass per hour basis by introducing particles of bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones, said bastnaesite particles being particles of natural bastnaesite or a treated natural bastnaesite containing at least some of its original fluorine.

Claim 8

In a cyclic catalytic cracking process wherein cracking catalyst particles comprising a crystalline aluminosilicate zeolite are continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with said circulating catalyst particles under conditions sufficient to convert said feedstock to more valuable hydrocarbons of lower average molecular weight and lower average boiling point than said feedstock while said catalyst particles become deactivated with coke deposits, and said catalyst particles are then passed through a regeneration zone and reactivated by burning said coke off said catalyst particles under conditions whereby a flue gas containing carbon monoxide and carbon dioxide is produced, and said catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the rate at which carbon monoxide in said flue gas is discharged from said regeneration zone on a mass per hour basis by introducing particles of bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones, said bastnaesite particles being particles of natural bastnaesite or a treated natural bastnaesite containing at least some of its original fluorine.

Claim 9

In a cyclic catalytic cracking process wherein cracking catalyst particles comprising a crystalline aluminosilicate zeolite are continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with said circulating catalyst particles under conditions sufficient to convert said feedstock to more valuable hydrocarbons of lower average molecular weight and lower average boiling point than said feed-stock while said catalyst particles become deactivated with coke deposits, and said catalyst particles are then passed through a regeneration zone and reactivated by burning said coke off said catalyst particles under conditions whereby a flue gas containing carbon monoxide and carbon dioxide is produced, and said catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the rate at which carbon monoxide in said flue gas is discharged from said regeneration zone on a mass per hour basis by introducing particles of natural bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones.

Claim 10

In a cyclic catalytic cracking process wherein cracking catalyst particles comprising a crystalline aluminosilicate zeolite are continuously circulated through a catalytic cracking reaction zone and a regeneration zone, and a hydrocarbon feedstock is fed to said catalytic cracking reaction zone and therein contacted at an elevated temperature with said circulating catalyst particles under conditions sufficient to convert said feedstock to more valuable hydrocarbons of lower average molecular weight and lower average boiling point than said feed-stock while said catalyst particles become deactivated with coke deposits, and said catalyst particles are then passed through a regeneration zone and reactivated by burning said coke off said catalyst particles under conditions whereby a flue gas containing carbon monoxide and carbon dioxide is produced, and said catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the rate at which carbon monoxide in said flue gas is discharged from said regeneration zone on a mass per hour basis by introducing particles of natural bastnaesite in with the catalyst particles continuously circulating through the catalytic cracking reaction and regeneration zones.

Claim 11

In a cyclical catalytic cracking process wherein a sulfur-containing hydrocarbon feedstock is fed to a catalytic cracking reaction zone and therein contacted with cracking catalyst particles at an elevated temperature, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are firstly passed through a stripping zone to convert some of the coke deposits to valuable gaseous products and then reactivated in a regeneration zone by burning most of said coke off said cracking catalyst particles thereby producing a flue gas containing CO and SO x compounds and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of CO and SO x compounds carried from said regeneration zone with said flue gas by introducing particles of bastnaesite into the catalytic cracking cycle, said bastnaesite particles being particles of natural bastnaesite or a treated natural bastnaesite containing at least some of its original fluorine.

Claim 12

In a cyclical catalytic cracking process wherein a sulfur-containing hydrocarbon feedstock is fed to a catalytic cracking reaction zone and therein contacted with cracking catalyst particles at an elevated temperature, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are firstly passed through a stripping zone to convert some of the coke deposits to valuable gaseous products and then reactivated in a regeneration zone by burning most of said coke off said cracking catalyst particles thereby producing a flue gas containing CO and SO x compounds and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising reducing the amount of CO and SO x compounds carried from said regeneration zone with said flue gas by introducing particles of bastnaesite into the catalytic cracking cycle, said bastnaesite particles being particles of natural bastnaesite or a treated natural bastnaesite containing at least some of its original fluorine.

Claim 13

In a cyclical catalytic cracking process wherein a sulfur-containing hydrocarbon feedstock is fed to a catalytic cracking reaction zone and therein contacted with cracking catalyst particles at an elevated temperature, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are firstly passed through a stripping zone to convert some of the coke deposits to valuable gaseous products and then reactivated in a regeneration zone by burning most of said coke off said cracking catalyst particles thereby producing a flue gas containing CO and SO x compounds and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising substantially reducing the amount of CO and SO x compounds carried from said regeneration zone with said flue gas by introducing particles of natural bastnaesite into the catalytic cracking cycle.

Claim 14

In a cyclical catalytic cracking process wherein a sulfur-containing hydrocarbon feedstock is fed to a catalytic cracking reaction zone and therein contacted with cracking catalyst particles at an elevated temperature, whereby said hydrocarbon feedstock is converted to product hydrocarbons while said catalyst particles become deactivated with sulfur-containing coke deposits, and said deactivated catalyst particles are firstly passed through a stripping zone to convert some of the coke deposits to valuable gaseous products and then reactivated in a regeneration zone by burning most of said coke off said cracking catalyst particles thereby producing a flue gas containing CO and SO x compounds and said cracking catalyst particles are then recycled to said catalytic cracking reaction zone, the improvement comprising substantially reducing the amount of CO and SO x compounds carried from said regeneration zone with said flue gas by introducing particles of natural bastnaesite into the catalytic cracking cycle.

Claim 15

A process as defined in claims 1, 2, 3, 4, 5, 6, or 7 wherein said catalyst particles recycled from said regeneration zone to said catalytic cracking reaction zone contain less than about 0.15 catalyst weight percent of coke.

Claim 16

A process as defined in claims 1, 2, 3, 4, 5, 6, or 7 wherein said particles of bastnaesite are integral with the catalyst particles.

Claim 17

A process as defined in claims 1, 2, 3, 4, 5, 6, or 7 wherein said catalyst particles and said bastnaesite particles, after leaving the catalytic cracking reaction zone, pass through a steam stripping zone wherein the coke on the catalyst particles is partially converted to a valuable, gaseous product.

Claim 18

A process as defined in claims 1, 2, 3, 4, or 5 wherein the circulating particles comprise particulate aggregates containing particles of bastnaesite and particles of a crystalline aluminosilicate zeolite having activity for cracking hydrocarbons at a temperature above about 750° F. dispersed in a matrix of a porous inorganic refractory oxide containing aluminum atoms.

Claim 19

A process as defined in claim 11 wherein said bastnaesite particles are natural bastnaesite and said zeolite particles have been ion exchanged to contain less than about 4.0 percent by weight alkali metals, calculated as the metals, and to contain hydrogen and rare earth element ions.

Claim 20

A process as defined in claims 1, 2, 3, 4, 5, 6, or 7 wherein said bastnaesite particles comprise between about 5.0 and 20% by weight of the total particulates of catalyst and bastnaesite circulating through the catalytic cracking reaction and regeneration zones.

Claim 21

A process as defined in claims 1, 2, 3, 4, 5, 6, or 7 wherein said bastnaesite particles are separate from said catalyst particles but are integral with a porous refractory oxide.

Claim 22

A process as defined in claim 14 wherein said bastnaesite particles are dispersed in a porous, inorganic refractory oxide matrix.