Fluid coking and gasification process

Claim 2

An integrated coking and gasification process comprising the steps of: (a) reacting a carbonaceous chargestock in a coking zone containing a bed of fluidized solids maintained at fluid coking conditions to produce a vapor phase product, including normally liquid hydrocarbons, and coke, said coke depositing on said fluidized solids; (b) introducing a portion of said solids with the coke deposit thereon to a first fluid bed gasification zone maintained at gasification conditions; (c) reacting said portion of solids in said first gasification zone with an oxygen-containing gas to produce a first gaseous stream and partially gasified coke and supplying heat from said first gasification zone to said coking zone; (d) introducing a portion of said partially gasified coke from said first gasification zone to a second fluid bed gasification zone maintained at gasification conditions, said partially gasified coke supplying heat to said second gasification zone; (e) reacting said portion of partially gasified coke in said second gasification zone with a gas comprising steam in the absence of added oxygen-containing gas to produce a second gaseous stream wherein said second gaseous stream has a higher heating value than the heating value of said first gaseous stream, and (f) recycling a portion of said partially gasified coke from said second gasification zone to said first gasification zone.

Claim 3

In the process of claim 1, the additional steps which comprise: passing a portion of said solids with the coke deposit resulting from step (a) from said coking zone to a heating zone operated at a temperature greater than said coking zone temperature to heat said portion of solids; recycling a first portion of heated solids from said heating zone to said coking zone and introducing a second portion of said heated solids to said first fluid bed gasification zone.

Claim 4

The process of claim 1 wherein said molecular oxygen-containing gas is air.

Claim 5

The process of claim 1 wherein said first gasification zone and said second gasification zone are each maintained at a temperature ranging from about 1500° F. to about 2000° F.

Claim 6

The process of claim 1 wherein said first gasification zone is maintained at a temperature ranging from about 1600° to about 1800° F. and said second gasification zone is maintained at a temperature ranging from about 1600° to about 1800° F.

Claim 7

The process of claim 1 wherein said coking conditions include a temperature ranging from about 850° F. to 1400° F.

Claim 8

The process of claim 1 wherein said coking conditions include a temperature ranging from about 900° F. to about 1200° F.

Claim 9

The process of claim 1 wherein said coking conditions include a pressure ranging from about 0 to 150 psig.

Claim 10

The process of claim 1 wherein said carbonaceous chargestock has a Conradson carbon content of at least about 5 weight percent.

Claim 11

The process of claim 1 wherein said carbonaceous chargestock has a Conradson carbon content of at least about 10 weight percent.

Claim 12

The process of claim 2 wherein said first gaseous stream produced in said first gasification zone is passed to said heating zone.

Claim 13

The process of claim 2 wherein a portion of solids is passed from said first gasification zone to said heating zone.

Claim 14

The process of claim 1 wherein said carbonaceous chargestock comprises a hydrocarbonaceous oil.

Claim 15

The process of claim 1 wherein said carbonaceous chargestock comprises coal.

Claim 16

An integrated coking and gasification process comprising the steps of: (a) reacting a carbonaceous chargestock in a coking zone containing a bed of fluidized solids maintained at fluid coking conditions, including a temperature ranging from about 850° F. to about 1400° F., to produce a vapor phase product, including normally liquid hydrocarbons, and coke, said coke depositing on said fluidized solids; (b) introducing a portion of said solids with the coke deposit thereon into a heating zone operated at a temperature greater than said coking zone temperature to heat said portion of solids; (c) recycling a first portion of heated solids from said heating zone to said coking zone; (d) introducing a second portion of said heated solids to a first fluid bed gasification zone maintained at gasification conditions, including a temperature ranging from about 1500° F. to about 2000° F.; (e) reacting said second portion of said heated solids in said first gasification zone with a molecular oxygen-containing gas to produce a first gaseous stream and partially gasified coke and supplying heat from said first gasification zone to said heating zone of step (b); (f) introducing a portion of said partially gasified coke from said first gasification zone to a second fluid bed gasification zone maintained at gasification conditions, including a temperature ranging from about 1500° F. to about 2000° F., said partially gasified coke supplying heat to said second gasification zone; (g) reacting said portion of partially gasified coke in said second gasification zone with a gas comprising steam to produce a second gaseous stream, said second gaseous stream comprising hydrogen and carbon monoxide wherein said second gaseous stream has a higher heating value then the heating value of said first gaseous stream, and (h) recycling a portion of said partially gasified coke from said second gasification zone to said first gasification zone.

Claim 17

An integrated coking and gasification process comprising the steps of: (a) reacting a carbonaceous chargestock in a coking zone containing a bed of fluidized solids maintained at fluid coking conditions, including a temperature ranging from about 850° F. to about 1400° F., to produce a vapor phase product, including normally liquid hydrocarbons, and coke, said coke depositing on said fluidized solids; (b) introducing a portion of said solids with the coke deposit thereon into a heating zone operated at a temperature greater than said coking zone temperature to heat said portion of solids; (c) recycling a first portion of heated solids from said heating zone to said coking zone; (d) introducing a second portion of said heated solids to a first fluid bed gasification zone maintained at gasification conditions, including a temperature ranging from about 1500° F. to about 2000° F.; (e) reacting said second portion of said heated solids in said first gasification zone with a molecular oxygen-containing gas to produce a first gaseous stream and partially gasified coke and supplying heat from said first gasification zone to said heating zone of step (b); (f) introducing a portion of said partially gasified coke from said first gasification zone to a second fluid bed gasification zone maintained at gasification conditions, including a temperature ranging from about 1500° F. to about 2000° F., said partially gasified coke supplying heat to said second gasification zone; (g) reacting said portion of partially gasified coke in said second gasification zone with a gas comprising steam to produce a second gaseous stream, said second gaseous stream comprising hydrogen and carbon monoxide wherein said second gaseous stream has a higher heating value then the heating value of said first gaseous stream, and (h) recycling a portion of said partially gasified coke from said second gasification zone to said first gasification zone.

Claim 18

The process of claim 15 wherein at least a portion of said first gaseous stream of step (e) is passed to said heating zone of step (b).

Claim 19

The process of claim 15 wherein said portion of partially gasified coke in said second gasification zone is reacted with a gas comprising steam and a molecular oxygen-containing gas.

Claim 20

The process of claim 17 wherein said molecular oxygen-containing gas is air.

Claim 21

The process of claim 15 wherein said portion of partially gasified coke in said second gasification zone is reacted with said gas comprising steam in the absence of added oxygen-containing gas.