Abstract: A catalytic cracking unit is disclosed which provides for separation and quenching of the effluent with a total kinetic residence time of from 0.1 to 0.6 seconds.

Abstract: A catalytic cracking unit is disclosed which provides for quenching of a riser reactor effluent downstream of a rough cut separator and upstream of a cyclone separator.

Abstract: A catalytic cracking unit is disclosed which provides for separation and quenching of a catalytic cracking effluent.

Abstract: There is disclosed an improved solids regeneration apparatus for hydrocarbon cracking. The apparatus comprises an entrained bed heater adapter for spouted bed circulation of solids.

Abstract: A gas-particulate solids separation assembly having a mixed phase solids-gas elongated inlet terminating in a divergent section and horizontally disposed cylcone separators downstream of the separator gas outlets adapted to receive quench oil.

Abstract: An apparatus for cracking hydrocarbon with hot particulate solids wherein a curtain of hot particulate solids is delivered to a thermal reactor through peripheral openings and hydrocarbon feed is delivered to the reactor through the curtain of hot particulate solids at an angle.

Abstract: A process for cracking hydrocarbon with hot particulate solids wherein a curtain of hot particulate solids is delivered to a thermal reactor through peripheral openings and hydrocarbon feed is delivered to the reactor through the curtain of hot particulate solids at an angle.

Abstract: An apparatus to serve as a valve to regulate the flow of particulate solids, from an upstream to a downstream location. The valve relies on pressure differential rather than moving mechanical parts. A plenum adjacent a chamber designed to accommodate a slumped mass of particulate solids receives fluid pressure and transmits the pressure to the slumped mass to move the particulate solids through an opening to a downstream location.

Abstract: An automatic pressure sensitive regulation assembly and process is provided for use with a non-mechanical particulate solids flow apparatus. The automatic pressure sensitive regulation assembly comprises first and second pressurized fluid distributors. The first pressurized fluid distributor provides incipient fluidization of the particulate solids in the vicinity of the automatic pressure sensitive regulation assembly and an attendant hydrostatic pressure. The second pressurized fluid distributor senses variations in the hydrostatic pressure as a function of the particulate solids level, and in response thereto directly varies the flow of pressurized fluids to the downstream end of the particulate solids flow apparatus to change the rate of flow of particulate solids at the same rate as received.

Abstract: The apparatus of the present invention is a gas distributor system for installation beneath a fluidized bed, said distributor system containing a sift trap chamber for accumulating solids filtering through the distributor plate gas inlet means. The apparatus contains no internal parts in direct contact with the fluidized bed, and thereby limits erosion of the distributor thus reducing greatly the cost of fabrication and maintenance.