Method and means for separating gaseous materials from finely divided catalyst particles

Claim 2

In a process for the fluid catalytic cracking of mineral oil whereby the mineral oil is catalytically cracked by passing a suspension of mineral oil and catalyst through a riser conversion zone under cracking conditions into a disengaging vessel and the catalyst recovered from said riser conversion zone is thereafter regenerated to remove carbonaceous deposits before return of the regenerated catalyst to said riser conversion zone and whereby the mineral oil-catalyst suspension is separated upon discharge from the riser conversion zone by (a) discharging the suspension outwardly through an opening in the upper periphery of the riser and through a radially extending restricted passageway having an opening in the bottom side thereof whereby a substantially confined catalyst stream discharges in a downward direction generally separate from the cracked mineral oil vapors, said restricted passageway curved downwardly adjacent the outer end thereof to induce a downward movement on said confined catalyst stream in said passageway sufficient to direct said stream downwardly into the open upper end of a catalyst stripping passageway positioned beneath said outer end to maintain catalyst so collected and directed separate from said discharged cracked mineral oil vapors and (b) passing the cracking mineral oil vapors through the disengaging vessel to the upper portion thereof and into the entrance of a cyclone separation means, the improvement which comprises: discharging the cracked mineral oil vapors from the outer extremity of the radially extending restricted passageway to a vertically disposed elongated restricted passageway in fluid communication with the inlet of a first cyclone separation means whereby the cracked mineral oil vapors are directed from the outer extremity of the radially extending restricted passageway into the first cyclone separation means.

Claim 3

A process according to claim 1 wherein the suspension of the cracked mineral oil vapors and the catalyst are discharged in a downward direction from the radially extending restricted passageway, whereby the catalyst passes to the catalyst stripping passageway and the cracked mineral oil vapors are combined with stripped hydrocarbons and stripping steam from the catalyst stripping passageway and pass through the vertically disposed restricted passageway into the cyclone separation means, said vertically disposed restricted passageway surrounding and containing the radially extending restricted passageway in spaced relationship thereto and in direct fluid communication with the upper end of the catalyst stripping passageway.

Claim 4

A process according to claim 1 wherein the catalyst and a minor portion of the cracked mineral oil vapors are discharged in a downward direction into the interior of the disengaging vessel and the remaining cracked mineral oil vapors are discharged in an upward direction into the vertically disposed restricted passageway, whereby, the catalyst passes into the catalyst stripping passageway, the minor portion is combined with stripped hydrocarbons and stripping steam from the catalyst stripping passageway to form a vaporous admixture, the vaporous admixture passes through the interior of the disengaging vessel and into a second cyclone separation means, and the remaining cracked mineral oil vapors pass through the vertically disposed restricted passageway into the first cyclone separation means, the lower end of the vertically disposed restricted passageway being in fluid communication with the outer extremity of the radially extending restricted passageway.

Claim 5

A process according to claim 1 wherein the cracked mineral oil vapors are cooled in the vertically disposed restricted passageway to a temperature below about 1000° F.

Claim 6

A process according to claim 4 wherein the cooling is effected by indirect heat exchange.

Claim 7

A process according to claim 4 wherein the cooling is effected by liquid or gaseous quench.

Claim 8

A process according to claim 2 wherein the cracked mineral oil vapors pass from the first cyclone separation means through a vapor conduit to a fractionation means.

Claim 9

A process according to claim 3 wherein the remaining cracked mineral oil vapors pass from the first cyclone separation means through a vapor conduit to a fractionation means and the vaporous admixture passes from the second cyclone separation means through a vapor conduit to a fractionation means.

Claim 12

An apparatus according to claim 9 wherein the vertically disposed restricted passageway additionally contains a cooling means.

Claim 13

An apparatus according to claim 10 wherein the cooling means is an indirect heat exchange means.

Claim 14

An apparatus according to claim 10 wherein the cooling means is a direct heat exchange means.

Claim 17

An apparatus according to claim 13 wherein the vertically disposed restricted passageway additionally contains a cooling means.

Claim 18

An apparatus according to claim 14 wherein the cooling means is an indirect heat exchange means.

Claim 19

An apparatus according to claim 14 wherein the cooling means is a direct heat exchange means.

Claim 20

An apparatus according to claim 13 including the following apparatus: a second cyclone separation means having an inlet communicating with the interior of said disengaging vessel and a gas outlet communicating with the exterior of said disengaging vessel.

Claim 21

In a process for the fluid catalytic cracking of mineral oil whereby the mineral oil is catalytically cracked by passing a suspension of mineral oil and catalyst through a riser conversion zone under cracking conditions into a disengaging vessel and the catalyst recovered from said riser conversion zone is thereafter regenerated to remove carbonaceous deposits before return of the regenerated catalyst to said riser conversion zone and whereby the mineral oil-catalyst suspension is separated upon discharge from the riser conversion zone by (a) discharging the suspension outwardly through an opening in the upper periphery of the riser and through a radially extending restricted passageway having an opening in the bottom side thereof whereby a substantially confined catalyst stream discharges in a downward direction generally separate from the cracked mineral oil vapors, said restricted passageway curved downwardly adjacent the outer end thereof to induce a downward movement on said confined catalyst stream in said passageway sufficient to direct said stream downwardly into the open upper end of a catalyst stripping passageway positioned beneath said outer end to maintain catalyst so collected and directed separate from said discharged cracked mineral oil vapors and (b) passing the cracking mineral oil vapors through the disengaging vessel to the upper portion thereof and into the entrance of a cyclone separation means, the improvement which comprises: discharging the cracked mineral oil vapors from the outer extremity of the radially extending restricted passageway to a vertically disposed restricted passageway in fluid communication with the inlet of a first cyclone separation means whereby the cracked mineral oil vapors are directed from the outer extremity of the radially extending restricted passageway into the first cyclone separation means and cooling mineral oil vapors in the vertically disposed restricted passageway to a temperature below about 1000° F.

Claim 22

In a process for the fluid catalytic cracking of mineral oil whereby the mineral oil is catalytically cracked by passing a suspension of mineral oil and catalyst through a riser conversion zone under cracking conditions into a disengaging vessel and the catalyst recovered from said riser conversion zone is thereafter regenerated to remove carbonaceous deposits before return of the regenerated catalyst to said riser conversion zone and whereby the mineral oil-catalyst suspension is separated upon discharge from the riser conversion zone by (a) discharging the suspension outwardly through an opening in the upper periphery of the riser and through a radially extending restricted passageway having an opening in the bottom side thereof whereby a substantially confined catalyst stream discharges in a downward direction generally separate from the cracked mineral oil vapors, said restricted passageway curved downwardly adjacent the outer end thereof to induce a downward movement on said confined catalyst stream in said passageway sufficient to direct said stream downwardly into the open upper end of a catalyst stripping passageway positioned beneath said outer end to maintain catalyst so collected and directed separate from said discharged cracked mineral oil vapors and (b) passing the cracking mineral oil vapors through the disengaging vessel to the upper portion thereof and into the entrance of a cyclone separation means, the improvement which comprises: discharging the cracked mineral oil vapors from the outer extremity of the radially extending restricted passageway to a vertically disposed restricted passageway in fluid communication with the inlet of a first cyclone separation means whereby the cracked mineral oil vapors are directed from the outer extremity of the radially extending restricted passageway into the first cyclone separation means and cooling mineral oil vapors in the vertically disposed restricted passageway to a temperature below about 1000° F.

Claim 25

An apparatus according to claim 19 wherein the cooling means is an indirect heat exchange means.

Claim 26

An apparatus according to claim 10 wherein the cooling means is a direct heat exchange means.