Power recovery process using recuperative heat exchange

Claim 2

A process for recovering energy from a high temperature flue gas stream of a catalyst regeneration zone of a fluidized catalytic cracking unit which comprises the steps of: (a) passing said high temperature flue gas stream having a superatmospheric pressure of between about 25 to 60 psig through a first indirect heat exchange means and cooling the gas stream to a temperature below about 400° C.; (b) passing the gas stream through a second indirect heat exchange means and cooling the gas stream to a temperature below 150° C.; (c) removing particles from the gas stream in a particle removal zone in which the gas stream is contacted with a liquid under conditions suitable for the transfer of particles from the gas stream to the liquid; (d) passing the gas stream through the second indirect heat exchange means and heating the gas stream to a temperature above 300° C. and within 50° to 70° of the temperature of the gas stream entering said second indirect heat exchange means in step (b); and (e) depressurizing the gas stream in a power recovery expander and thereby recovering useful mechanical energy from the gas stream.

Claim 3

The process of claim 1 further characterized in that the gas stream is heated to a temperature between about 300° C. and about 375° C. in step (d).

Claim 4

The process of claim 2 further characterized in that the liquid with which the gas stream is contacted in the particle removal zone is water.

Claim 5

The process of claim 2 further characterized in that the liquid with which the gas stream is contacted in the particle removal zone comprises a mixture of hydrocarbonaceous compounds having a 10 percent boiling point above 260° C.

Claim 6

The process of claim 1 further characterized in that the gas stream is heated in the catalyst regeneration zone by indirect heat exchange after having passed through the particle removal zone and having been heated in the second indirect heat exchange means but prior to the depressurization of the gas stream in the power recovery expander.

Claim 7

A process for recovering energy from a superatmospheric pressure flue gas stream of a catalyst regeneration zone of a fluidized catalytic cracking unit which comprises the steps of: (a) cooling said superatmospheric pressure flue gas stream removed from said FCC catalyst regeneration zone having a pressure of between about 25 and 60 psig to a temperature between 260° C. and 380° C. by passage through a first indirect heat exchange means in which steam is produced; (b) further cooling said flue gas stream to a temperature below about 105° C. in a second indirect heat exchange means; (c) passing the flue gas stream after passage through said second indirect heat exchange means through a particle removal zone in which catalyst particles are removed from the flue gas stream by contact with a liquid under conditions suitable for the transfer of catalyst particles from the flue gas stream to the liquid; (d) heating said flue gas stream from said particle removal zone of step (c) in said second indirect heat exchange means to a temperature above 330° C. and within 50°-70° C. of said temperature range of 260° C. to 380° C. of step (a); and, (e) passing said heated flue gas stream of step (d) through a power recovery expander in which the pressure of the flue gas stream is reduced.

Claim 8

A process for recovering energy from a superatmospheric pressure flue gas stream of a catalyst regeneration zone of a fluidized catalytic cracking unit which comprises the steps of: (a) cooling said superatmospheric pressure flue gas stream removed from said FCC catalyst regeneration zone having a pressure of between about 25 and 60 psig to a temperature between 260° C. and 380° C. by passage through a first indirect heat exchange means in which steam is produced; (b) further cooling said flue gas stream to a temperature below about 105° C. in a second indirect heat exchange means; (c) passing the flue gas stream after passage through said second indirect heat exchange means through a particle removal zone in which catalyst particles are removed from the flue gas stream by contact with a liquid under conditions suitable for the transfer of catalyst particles from the flue gas stream to the liquid; (d) heating said flue gas stream from said particle removal zone of step (c) in said second indirect heat exchange means to a temperature above 330° C. and within 50°-70° C. of said temperature range of 260° C. to 380° C. of step (a); and, (e) passing said heated flue gas stream of step (d) through a power recovery expander in which the pressure of the flue gas stream is reduced.

Claim 9

The process of claim 6 further characterized in that the flue gas stream is heated by indirect heat exchange after having passed through the particle removal zone and having been heated in the second indirect heat exchange means.

Claim 10

The process of claim 6 further characterized in that the liquid used in the particle removal zone is a hydrocarbonaceous liquid having a 10 percent boiling point above 260° C.

Claim 11

The process of claim 8 further characterized in that the flue gas stream is passed into a combustion zone after having passed through the power recovery expander.

Claim 12

The process of claim 6 further characterized in that the liquid used in the particle removal zone is water.