Cogeneration process linking FCC regenerator and power plant turbine

Claim 2

A process for generating electrical power which comprises the steps of: (a) producing a pressurized air stream by compressing air to a superatmospheric pressure in a compressor driven by a power recovery expander which receives as a motive stream the flue gas stream of the catalyst regeneration zone of a fluidized catalytic cracking unit; (b) heating the pressurized air stream by indirect heat exchange; and, (c) passing the pressurized air stream and a high temperature gas stream through a turbine which drives an electrical generator and thereby producing a turbine effluent stream.

Claim 3

The process of claim 1 further characterized in that the pressurized air stream is heated by indirect heat exchange in step (b) against the turbine effluent stream.

Claim 4

The process of claim 2 further characterized in that the high temperature gas stream is produced by one or more turbine-type gas generators.

Claim 5

The process of claim 3 further characterized in that the pressurized air stream is admixed with the high temperature gas stream.

Claim 6

An air supply system for the catalyst regeneration zone of a fluidized catalytic cracking unit which comprises: (a) a first air compressor operably connected to a first drive means; (b) a second air compressor operably connected to a second drive means which comprises a flue gas power recovery expander which receives the flue gas of a catalyst regeneration zone of a fluidized catalytic cracking unit; (c) a turbine operably connected to an electrical generator; (d) a first air duct means connecting the first air compressor to the catalyst regeneration zone; (e) a second air duct means connecting the second air compressor to the turbine; (f) a third air duct means connecting the first air duct means and the second air duct means; and, (g) a flow control means comprising a valve means selectively capable of restricting air flow in the second or the third air duct means and also including a control means which activates the valve means if the first air compressor fails to supply sufficient air to the catalyst regeneration zone through the first air duct means.

Claim 7

An air supply system for the catalyst regeneration zone of a fluidized catalytic cracking unit which comprises: (a) a first air compressor operably connected to a first drive means; (b) a second air compressor operably connected to a second drive means which comprises a flue gas power recovery expander which receives the flue gas of a catalyst regeneration zone of a fluidized catalytic cracking unit; (c) a turbine operably connected to an electrical generator; (d) a first air duct means connecting the first air compressor to the catalyst regeneration zone; (e) a second air duct means connecting the second air compressor to the turbine; (f) a third air duct means connecting the first air duct means and the second air duct means; and, (g) a flow control means comprising a valve means selectively capable of restricting air flow in the second or the third air duct means and also including a control means which activates the valve means if the first air compressor fails to supply sufficient air to the catalyst regeneration zone through the first air duct means.

Claim 8

The air supply system of claim 5 further characterized in that a high temperature gas generating means is also operably connected to the turbine.

Claim 9

A cogeneration process which comprises the steps of: (a) contacting a feed stream comprising hydrocarbonaceous compounds having an atmospheric boiling point above 350° F. with a particulate catalyst within the reaction zone of a fluidized catalytic cracking unit; (b) passing used catalyst into the catalyst regeneration zone of the fluidized catalytic cracking unit from the reaction zone; (c) compressing air in a first compressor and forming a first air stream which is passed into the catalyst regeneration zone of the fluidized catalytic cracking unit for use in burning carbon present on the catalyst within the catalyst regeneration zone; (d) passing a flue gas stream, which is removed from the regeneration zone of the fluidized catalytic cracking unit, and which comprises nitrogen and carbon dioxide through a power recovery expander in which the flue gas stream is depressurized, and thereby generating motive force which is used to drive a second compressor, with the second compressor producing a second air stream having a superatmospheric pressure; (e) heating the second air stream by indirect heat exchange against a hereinafter characterized turbine effluent stream; and, (f) passing the second air stream and a high temperature gas stream through a turbine which drives an electrical generator and thereby producing said turbine effluent stream.

Claim 10

A cogeneration process which comprises the steps of: (a) contacting a feed stream comprising hydrocarbonaceous compounds having an atmospheric boiling point above 350° F. with a particulate catalyst within the reaction zone of a fluidized catalytic cracking unit; (b) passing used catalyst into the catalyst regeneration zone of the fluidized catalytic cracking unit from the reaction zone; (c) compressing air in a first compressor and forming a first air stream which is passed into the catalyst regeneration zone of the fluidized catalytic cracking unit for use in burning carbon present on the catalyst within the catalyst regeneration zone; (d) passing a flue gas stream, which is removed from the regeneration zone of the fluidized catalytic cracking unit, and which comprises nitrogen and carbon dioxide through a power recovery expander in which the flue gas stream is depressurized, and thereby generating motive force which is used to drive a second compressor, with the second compressor producing a second air stream having a superatmospheric pressure; (e) heating the second air stream by indirect heat exchange against a hereinafter characterized turbine effluent stream; and, (f) passing the second air stream and a high temperature gas stream through a turbine which drives an electrical generator and thereby producing said turbine effluent stream.

Claim 11

The process of claim 7 further characterized in that the second air stream is admixed with the high temperature gas stream and then passed into the turbine.

Claim 12

The process of claim 8 further characterized in that the first compressor is driven by steam which is heated within the catalyst regeneration zone of the fluidized catalytic cracking unit.

Claim 13

The process of claim 8 further characterized in that the first compressor is driven by steam produced by indirect heat exchange performed within the catalyst regeneration zone of the fluidized catalytic cracking unit.

Claim 14

The process of claim 10 further characterized in that at least 60 vol.% of the feed stream has an atmospheric boiling point above 650° F.

Claim 15

The process of claim 8 further characterized in that heat is removed from the regeneration zone of the fluidized catalytic cracking unit through the production of steam having a temperature above 500° F. and at least a portion of this steam is used to drive the first compressor.

Claim 16

The process of claim 8 further characterized in that the second air stream is heated after the indirect heat exchange of step (e) by direct combustion with an added fuel and is then admixed with the high temperature gas stream.