Abstract Accordingly, the present invention, in one embodiment, encompasses an apparatus for the fluidized catalytic cracking of a hydrocarbon feed comprising: a riser which is generally vertically positioned within a catalyst disengaging zone and which has a plurality of openings around the circumference of the riser at its discharge end. The openings in the riser have a vertical stub portion that extends tangentially outwardly from the riser and communicates with a first end of an upwardly sloping curvilinear tunnel that terminates at a second end. The second end of the tunnel opens into a tangential opening in the primary cyclone. The area of the opening of the first end of the tunnel is larger than the area of the opening of the second end of the tunnel.
In the method of separating entrained solids from a gaseous phase by guiding the mixture from a vertically disposed riser within a vessel to at least one cyclone separator, the improvement comprising: increasing the acceleration of the mixture as it is guided from the riser to the cyclone separator whereby the mixture enters the cyclone at a velocity sufficient to provide improved separation of solids from the gaseous phase.
Claim 2
Dependent Claim
69 words
In the method of separating entrained solids from a gaseous phase by guiding the mixture from a vertically disposed riser within a vessel to at least one cyclone separator, the improvement comprising: increasing the acceleration of the mixture as it is guided from the riser to the cyclone separator whereby the mixture enters the cyclone at a velocity sufficient to provide improved separation of solids from the gaseous phase.
Claim 3
Dependent Claim
24 words
The improvement of claim 1 wherein the mixture is guided substantially tangentially outward from the riser and upwardly and arcuately toward the cyclone separator.
Claim 4
Dependent Claim
23 words
The improvement of claim 2 wherein the mixture is guided through a flow path which decreases from the riser to the cyclone separator.