Reactor for the conversion of hydrocarbons and method
A reactor ( 12 ) and method for the conversion of hydrocarbons utilizes a reactor ( 12 ) having a unique feed assembly ( 56 ) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a conduit ( 46 ) with a constricted neck portion or nozzle ( 52 ). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the conduit ( 46 ). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the conduit ( 46 ) for conversion of hydrocarbons.
1 . A reactor for the conversion of hydrocarbons, the reactor comprising:
a reactor vessel that defines a reaction chamber;
a smoothly-tapering, converging, and diverging conduit in fluid communication with the reaction chamber, where the conduit comprises a central axis that extends along the conduit;
a feed assembly comprising a central chamber through which the central axis passes and that is in fluid communication with the conduit, wherein the feed assembly comprises flow spaces each having an annular shape configured to (i) separately introduce feeds comprising a hydrocarbon feed and a gas feed radially inward into the central chamber and (ii) to form a swirling fluid flow pattern about the central axis so that the feeds are mixed together to form a swirling gas mixture within the central chamber, whereby a portion of the swirling gas mixture is combusted to heat the swirling gas mixture and the heated swirling gas mixture passes through the conduit at flow velocities from 500 m/s or less where the hydrocarbon feed is converted into a converted hydrocarbon product, and wherein a recirculation zone in the reaction chamber is formed by a back flow of flue gases produced from the combustion of the swirling gas mixture; and
an outlet for removing the converted hydrocarbon product from the reaction chamber.
2 . The reactor of claim 1 , wherein the feed assembly comprises guide vanes and/or inlets oriented so the feeds are introduced in the same or substantially the same angular pattern.
3 . The reactor of claim 1 , wherein at least one of the flow spaces comprises circumferentially spaced apart guide vanes oriented to facilitate forming the swirling fluid flow pattern.
4 . The reactor of claim 3 , wherein the guide vanes are each movable to selected positions to provide selected azimuthal-to-radial velocity ratios of the feed within the at least one of the flow spaces.
5 . The reactor of claim 1 , wherein at least one of the flow spaces comprise inlets oriented to facilitate forming the swirling fluid flow pattern.
6 . The reactor of claim 1 , wherein at least one of the flow spaces is provided with one or more inlets and/or guide vanes oriented to provide an azimuthal-to-radial velocity ratio from 0 to 30.
7 . The reactor of claim 1 , wherein at least one of the flow spaces comprises one or more inlets and/or guide vanes oriented at an angle relative to a radial line extending from the central axis, with the angle ranging from 50° to 85° to facilitate forming the swirling flow pattern.
8 . The reactor of claim 1 , wherein the reaction chamber is cylindrical in shape.
9 . The reactor of claim 1 , wherein an interior of the reaction chamber comprises a refractory material.
10 . The reactor of claim 1 , wherein the flow spaces are separated by at least one partition wall with a central opening that partially defines the central chamber.
11 . The reactor of claim 1 , wherein the reactor comprises a subsonic reactor.
12 . The reactor of claim 1 , wherein the reactor does not use an exterior cooling jacket to cool the reactor vessel.
13 . The reactor of claim 1 , further comprising:
a quenching unit configured to quench the converted hydrocarbon product.
14 . A reactor for the conversion of hydrocarbons, the reactor comprising:
a reactor vessel that defines a reaction chamber;
a burner assembly comprising a smoothly-tapered conduit in fluid communication with the reaction chamber, where the conduit comprises (i) a central axis that extends along the conduit and (ii) a constricted neck portion;
a feed assembly comprising a central chamber through which the central axis passes and that is in fluid communication with the conduit, wherein the feed assembly comprises annular flow spaces configured to (i) separately introduce feeds comprising a hydrocarbon feed and an oxygen-containing gas feed radially inward into the central chamber and (ii) to form a swirling fluid flow pattern about the central axis so that the feeds are mixed together to form a swirling gas mixture within the central chamber, whereby a portion of the swirling gas mixture is combusted to heat the swirling gas mixture and the swirling gas mixture passes through the constricted neck portion of the conduit at flow velocities from 500 m/s or less where the hydrocarbon feed is converted into a converted hydrocarbon product, and wherein the constricted neck portion has a geometry configured to provide a recirculation zone in the reaction chamber that is formed by a back flow of flue gases produced from the combustion of the swirling gas mixture;
wherein at least one of the annular flow spaces comprises one or more inlets and/or guide vanes oriented to facilitate forming the swirling fluid flow pattern; and
an outlet for removing the converted hydrocarbon product from the reaction chamber.
15 . The reactor of claim 14 , wherein the reaction chamber is cylindrical in shape.
16 . The reactor of claim 14 , wherein an interior of the reactor vessel comprises a refractory material.
17 . The reactor of claim 14 , wherein the reactor does not use an exterior cooling jacket to cool the reactor vessel.