Abstract: An apparatus for fluid catalytic cracking (FCC) wherein the output of a reactor riser zone is fed to a riser cyclone separator, a primary cyclone separator, and secondary cyclone separators, connected in series within a single reactor vessel. The riser cyclone separator is connected to the primary cyclone separator by a conduit, which prevents random post-riser thermal cracking of the hydrocarbons after they exit the riser cyclone separator. The conduit contains an annular port to allow stripping gas to enter the conduit to improve the separation of hydrocarbons from catalyst. Catalyst separated in the riser cyclone separator drops through a riser cyclone dipleg and passes through a dipleg seal which comprises a seal pot or catalyst held around the dipleg. The conduit is formed by two overlapping parts, one having a larger diameter than the other to form the annular port and packing or spacers may be used to align and space the overlapping parts.

Abstract: A method and apparatus for improving the flow of catalyst particles from a riser conversion zone to a separator in a fluidized catalytic cracking (FCC) unit. The exit of the riser conversion zone is equipped with a deflector mounted so as to redirect catalyst particle and gas suspension movement toward a separator inlet, thus preventing rebound back into the riser conversion zone. The catalyst deflector, in other embodiments, can be combined with one or more of a short contact time stripper, a stripper mount in or adjacent the exhaust barrel of a separator, and/or a catalyst seal pot, all serving to reduce "residence" time of hydrocarbons with catalyst particles.

Abstract: Disclosed is a method and apparatus for fluid catalytic cracking (FCC). The output of a riser conversion zone is fed to a riser cyclone separator, a primary cyclone separator, and secondary cyclone separator, connected in series within a single reactor vessel. The riser cyclone separator is connected to the primary cyclone separator by a conduit which prevents random post-riser thermal cracking of the hydrocarbons after they exit the riser cyclone. Means are also provided to blend stripping gas with the cracked hydrocarbons as they travel from the riser conversion zone to said primary cyclone separator. The stripping gas blends with the cracked hydrocarbons to improve the separation of hydrocarbons from catalyst. Steam may also be directly injected into the riser cyclone separator to aid in separation of hydrocarbons from catalyst.

Abstract: A method and apparatus for improving the separation of a catalyst phase from a gas suspension phase in a fluidized catalytic cracking (FCC) unit. In a vertical separation embodiment, a cyclone separator inlet is located in the upper portion of a riser conversion zone and draws off gaseous hydrocarbon materials, while catalyst particles continue vertically to the end of the riser conversion zone, and pass through a catalyst conduit to a catalyst storage area. In a horizontal separation embodiment, the catalyst/hydrocarbon mixture is transported horizontally from the end of the riser conversion zone past a cyclone separator inlet towards a catalyst conduit. The cyclone inlet draws off gaseous hydrocarbon materials, while the catalyst particles pass through the catalyst conduit to a catalyst storage area.

Abstract: A method and apparatus for improving the stripping of hydrocarbons from catalyst particles in a fluidized catalytic cracking (FCC) unit. A stripper vessel has catalyst particles entering at one end and stripped catalyst particles exiting at another end. While passing through the stripper, the catalyst particles are exposed to a stripping gas, in a preferred embodiment steam, at each stage. A baffle and conduit system is provided, such that after exposure to only a portion of catalyst contained above the steam injection location in the stripper, the stripping gas and any stripped hydrocarbons are removed from any further substantial catalyst contact. The short contact time (SCT) stripper, in other embodiments, can be combined with one or more of a riser conversion zone deflector, a stripper mount in or adjacent the exhaust barrel of a separator, and/or a catalyst seal pot, all serving to reduce "residence" time of hydrocarbons with catalyst particles.

Abstract: A process and apparatus for direct coking of tar sands which includes contacting the tar sand with heat transfer particles resulting from combustion of coked sand effluent from the coking process, and transporting the combination up a riser/mixer to a coking vessel whereby separation of oil and hydrocarbon gases from the sand is initiated. The tar sand is introduced into a fluid coking vessel which has at least two coking zones. The first coking zone is substantially at the top of the vessel whereas the second coking zone is immediately below the first coking zone and includes a stream of hot spent sand so that a more severe coking temperature is present in the second coking zone. A product stream of oil and light hydrocarbon gases, recovered from the riser/mixer and coking process, is directed to a separator located above said coking vessel in which the heavy oil is removed and preferably directed to the second coking zone.

Abstract: A fast fluidized bed regenerator of an FCC apparatus is improved by incorporating into the regenerator an internal riser, for more complete combustion of coke, and by providing a means of preventing catalyst flow reversals between the spent and regenerated beds of the catalyst.

Abstract: A dropout boot is provided for removing solid particles from a hot gas stream comprising an enclosed metal boot shell having an upper vertical inlet means adapted to receive hot gas from refractory lined gas conduit and having a lower horizontal outlet means for passing hot clean gas to an energy recovery system or the like; said boot shell having an upper flared portion adjacent the inlet means with outward and downwardly flared configuration whereby gas velocity is substantially reduced in the boot shell; a shell floor having open bottom horizontal baffle means for retaining solid particles from the gas; said outlet means having an inwardly extending portion with an upper horizontal overhang protruding into the boot shell below the flared portion and inlet means; and an outlet grating mounted over the horizontal outlet transversely of gas flow below the outlet overhang portion and sloped outwardly and downwardly therefrom.

Abstract: Disclosed is a method and apparatus for fluid catalytic cracking (FCC). The output of a reactor riser zone is fed to a riser cyclone separator, a primary cyclone separator, and secondary cyclone separators, connected in series within a single reactor vessel. The riser cyclone separator is connected to the primary cyclone separator by a conduit, which prevents random post-riser thermal cracking of the hydrocarbons after they exit the riser cyclone separator. The conduit contains an annular port to allow stripping gas to enter the conduit to improve the separation of hydrocarbons from catalyst. Catalyst separated in the riser cyclone separator drops through a riser cyclone dipleg and passes through a dipleg seal which comprises a seal pot or catalyst held around the dipleg. The conduit is formed by two overlapping parts, one having a larger diameter than the other to form the annular port and packing or spacers may be used to align and space the overlapping parts.

Abstract: A fast fluidized bed regenerator of an FCC apparatus is improved by incorporating into the regenerator an internal riser, for more complete combustion of coke, and by providing a means of preventing catalyst flow reversals between the spent and regenerated beds of the catalyst.

Abstract: A fluid catalytic cracking vessel having cyclone separators which have cyclone diplegs. The diplegs have valve plates which are inclined, in the closed position, at an angle of about 30.degree. to about 60.degree. with respect to the vertical axis of the respective diplegs.

Abstract: Alcohols and related oxygenates are converted in a riser reactor and dense fluid catalyst bed comprising ZSM-5 type catalyst circulated through a plurality of satellite stripping-cooling zones for temperature control. Catalyst utilized comprises from 5 to 30 weight percent coke for activity and selectivity control promoting the formation of olefins and aromatics at temperatures below about 427.degree. C. (800.degree. F.).

Abstract: Apparatus and method of its utilization for controlling exothermic reactions such as the conversion of methanol to either olefin-enriched or gasoline boiling range hydrocarbons are disclosed. More particularly, the arrangement of fluid catalyst bed apparatus can be employed under varying reaction conditions in order to adjust contact between vaporous reactant and fluidized catalyst so as to maximize production as desired of either gasoline boiling range products or olefinic products useful as chemical feedstocks.

Abstract: A suspension of catalyst and gasiform material is separated by a catalyst particle concentrating means which discharges the catalyst into a steam stripping zone and transmits the separated gasiform material to a cyclone separator by means of a restricted passageway which minimizes the time the gasiform material is exposed to the catalytic reaction product temperature.

Abstract: Alcohols and related oxygenates converted in a riser reactor and dense fluid catalyst bed (ZSM-5 cat), along with the catalyst, are circulated through a plurality of satellite stripping-cooling zones for temperature control. Catalyst utilized comprises from 5 to 20 weight percent coke for activity and selectivity characteristics promoting the formation of olefins and aromatics at temperatures below 800.degree. F.

Abstract: Apparatus and method of utilization for controlling exothermic reactions such as the conversion of methanol to hydrocarbons are discussed. More particularly, the arrangement of apparatus comprising heat exchange tubes and open end baffle tubes for maintaining the hydraulic diameter within restricted limits during contact between vaporous reactant and a fluid bed of catalyst is discussed.

Abstract: Alcohols and related oxygenates are converted in a riser reactor and dense fluid catalyst bed (ZSM-5 zeolite catalyst) circulated through a plurality of satellite stripping-cooling zones for temperature control. Catalyst utilized comprises from 5 to 20 weight percent coke for activity and selectivity characteristics promoting the formation of olefins and aromatics at temperatures below about 427.degree. C. (800.degree. F.).

Abstract: Apparatus and method of utilization for controlling exothermic reactions such as the conversion of methanol to hydrocarbons are discussed. More particularly, the arrangement of apparatus comprising heat exchange tubes and open end baffle tubes for maintaining the hydraulic diameter within restricted limits during contact between vaporous reactant and a fluid bed of catalyst is discussed.

Abstract: Alcohols and related oxygenates converted in a riser reactor and dense fluid catalyst bed (ZSM-5 cat) circulated through a plurality of satellite stripping-cooling zones for temperature control. Catalyst utilized comprises from 5 to 20 weight percent coke for activity and selectivity characteristics promoting the formation of olefins and aromatics at temperatures below 800.degree. F.

Abstract: A riser cracking-catalyst regeneration operation is described wherein a suspension discharged from a riser operation is separated by catalyst particle concentrating means which discharge a concentrated stream of catalyst separated from gasiform material into a downcomer zone and out of further contact with discharged gasiform material in the suspension. A stripping gas is used to particularly aid the separation of catalyst and hydrocarbon vapors.