Catalytic cracking process

Claim 2

In a fluid catalytic cracking unit comprising a cracking zone operating in the absence of added hydrogen and a catalyst regeneration zone designed to substantially completely combust carbon monoxide to carbon dioxide thermally; which unit contains a circulating inventory of solid acidic cracking catalyst, the improvement in the operation thereof, whereby the regenerator dense bed temperature is increased, which comprises: circulating with said catalyst a trace amount of at least one metal of the group consisting of platinum, palladium, iridium, osmium, rhodium, ruthenium and rhenium wherein the amount of said metal is from 0.01 to 50 ppm, based on total catalyst inventory.

Claim 3

The improvement of claim 1 wherein said regeneration zone includes a riser for carrying regenerated catalyst upwardly from a dense bed under conditions conducive to oxidation of carbon monoxide.

Claim 4

The improvement of claim 1 wherein the regeneration zone comprises a bottom chamber containing a dense bed, a riser in which regenerated catalyst is carried upwardly from the dense bed under conditions conducive to oxidation of carbon monoxide, and an upper chamber in which flue gas is separated from hot regenerated catalyst.

Claim 5

The improvement of claim 1 wherein combustion of carbon monoxide to carbon dioxide takes place in the dense bed of said regeneration zone.

Claim 6

The improvement of claim 1 wherein the amount of metal is under 10 ppm based on total catalyst inventory.

Claim 7

In a process for fluid catalytic cracking of hydrocarbons in the absence of added hydrogen in a cracking unit having a catalyst regeneration zone designed to substantially completely combust carbon monoxide to carbon dioxide thermally which process comprises cofeeding active hot solid cracking catalyst and crackable hydrocarbon feed to a cracking zone; cracking said feed to lighter hydrocarbons while depositing coke on said catalyst and cooling said catalyst; disengaging said cooled coked catalyst from said lighter hydrocarbon products; passing said coked catalyst to said regeneration zone; introducing an oxygen containing gas to said regeneration zone; reacting said gas and said coked catalyst in said regeneration zone at a temperature and for a time sufficient to burn coke off said catalyst, heat and regenerate such, and combust CO to CO 2 ; and returning said reactivated, heated catalyst to said cracking zone; the improvement, whereby the regenerator dense bed temperature is increased, which comprises: circulating with said catalyst a trace amount of at least one metal of the group consisting of platinum, palladium, iridium, osmium, rhodium, ruthenium and rhenium wherein the amount of said metal is from 0.01 to 50 ppm, based on total catalyst.

Claim 8

In a process for fluid catalytic cracking of hydrocarbons in the absence of added hydrogen in a cracking unit having a catalyst regeneration zone designed to substantially completely combust carbon monoxide to carbon dioxide thermally which process comprises cofeeding active hot solid cracking catalyst and crackable hydrocarbon feed to a cracking zone; cracking said feed to lighter hydrocarbons while depositing coke on said catalyst and cooling said catalyst; disengaging said cooled coked catalyst from said lighter hydrocarbon products; passing said coked catalyst to said regeneration zone; introducing an oxygen containing gas to said regeneration zone; reacting said gas and said coked catalyst in said regeneration zone at a temperature and for a time sufficient to burn coke off said catalyst, heat and regenerate such, and combust CO to CO 2 ; and returning said reactivated, heated catalyst to said cracking zone; the improvement, whereby the regenerator dense bed temperature is increased, which comprises: circulating with said catalyst a trace amount of at least one metal of the group consisting of platinum, palladium, iridium, osmium, rhodium, ruthenium and rhenium wherein the amount of said metal is from 0.01 to 50 ppm, based on total catalyst.

Claim 9

The process of claim 6 wherein the amount of metal circulating with said catalyst is under 10 ppm based on total catalyst.