Process for regenerating spent cracking catalyst

Claim 2

Process for regenerating deactivated cracking catalyst which has become deactivated in a hydrocarbon cracking process which comprises subjecting a mixture of deactivated cracking catalyst and hydrogen to microwave energy at a temperature of from 700° F. to 950° F. for a time of not more than ten minutes, and reusing the regenerated catalyst in said hydrocarbon cracking process.

Claim 3

Process according to claim 1 wherein the cracking catalyst has become deactivated in a fluidized cracking process for petroleum hydrocarbons.

Claim 4

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises fluidizing the deactivated catalyst with hydrogen and subjecting the fluidized catalyst-hydrogen mixture to microwave energy at a temperature of from 700° F. to 950° F. for a time of not more than ten minutes, and reusing the reactivated catalyst having a reduced coke content in said cracking operation.

Claim 5

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises fluidizing the deactivated catalyst with hydrogen and subjecting the fluidized catalyst-hydrogen mixture to microwave energy at a temperature of from 700° F. to 950° F. for a time of not more than ten minutes, and reusing the reactivated catalyst having a reduced coke content in said cracking operation.

Claim 6

Process according to claim 3 wherein the microwave energy is from about 1 to about 1,000,000 megacycles per second.

Claim 7

Process according to claim 4 wherein hydrocarbons are recovered from the regenerator.

Claim 8

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises forming a slurry of the catalyst particles and a solvent containing dissolved hydrogen and subjecting the slurry to microwave energy wherein said solvent is a petroleum distillate and the subjecting of the slurry to microwave energy is performed at a temperature of from 200° F. to 400° F., and returning regenerated catalyst particles to said hydrocarbon cracking operation.

Claim 9

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises forming a slurry of the catalyst particles and a solvent containing dissolved hydrogen and subjecting the slurry to microwave energy wherein said solvent is a petroleum distillate and the subjecting of the slurry to microwave energy is performed at a temperature of from 200° F. to 400° F., and returning regenerated catalyst particles to said hydrocarbon cracking operation.

Claim 10

Process according to claim 6 wherein the microwave energy is from about 1 to about 1,000,000 megacycles per second.

Claim 11

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises fluidizing the deactivated catalyst with hydrogen and subjecting the fluidized catalyst-hydrogen mixture to microwave energy wherein said microwave energy is composed of at least two different microwave frequencies, wherein the temperature is from 700° F. to 950° F. and the time of subjecting said mixture to microwave energy is from fifteen seconds to three minutes, and returning regenerated catalyst to said hydrocarbon cracking operation.

Claim 12

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises fluidizing the deactivated catalyst with hydrogen and subjecting the fluidized catalyst-hydrogen mixture to microwave energy wherein said microwave energy is composed of at least two different microwave frequencies, wherein the temperature is from 700° F. to 950° F. and the time of subjecting said mixture to microwave energy is from fifteen seconds to three minutes, and returning regenerated catalyst to said hydrocarbon cracking operation.

Claim 13

Process according to claim 8 wherein the fluidized catalyst-hydrogen mixture is subjected to at least two microwave frequencies simultaneously.

Claim 14

Process according to claim 8 wherein the fluidized catalyst-hydrogen mixture is subjected to at least two microwave frequencies consecutively.

Claim 15

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises forming a slurry of the catalyst particles and a solvent containing dissolved hydrogen and subjecting the slurry to microwave energy wherein said microwave energy is composed of at least two different microwave frequencies, wherein said solvent is a petroleum distillate, the temperature is above 200° F. and below the boiling point of the solvent, and the time of exposure to said microwave energy is from ten seconds to ten minutes, and returning reactivated cracking catalyst to said hydrocarbon cracking operation.

Claim 16

Process for regenerating fluidized cracking catalyst deactivated by coke formed in a hydrocarbon cracking operation which comprises forming a slurry of the catalyst particles and a solvent containing dissolved hydrogen and subjecting the slurry to microwave energy wherein said microwave energy is composed of at least two different microwave frequencies, wherein said solvent is a petroleum distillate, the temperature is above 200° F. and below the boiling point of the solvent, and the time of exposure to said microwave energy is from ten seconds to ten minutes, and returning reactivated cracking catalyst to said hydrocarbon cracking operation.

Claim 17

Process according to claim 11 wherein the fluidized catalyst-hydrogen mixture is subjected to at least two microwave frequencies simultaneously.

Claim 18

Process according to claim 11 wherein the slurry is subjected to at least two microwave frequencies consecutively.