초록 ▼

An apparatus for thermal conversion of one or more reactants to desired end products includes an insulated reactor chamber having a high temperature heater such as a plasma torch at its inlet end and, optionally, a restrictive convergent-divergent nozzle at its outlet end. In a thermal conversion m

An apparatus for thermal conversion of one or more reactants to desired end products includes an insulated reactor chamber having a high temperature heater such as a plasma torch at its inlet end and, optionally, a restrictive convergent-divergent nozzle at its outlet end. In a thermal conversion method, reactants are injected upstream from the reactor chamber and thoroughly mixed with the plasma stream before entering the reactor chamber. The reactor chamber has a reaction zone that is maintained at a substantially uniform temperature. The resulting heated gaseous stream is then rapidly cooled by passage through the nozzle, which "freezes" the desired end product(s) in the heated equilibrium reaction stage, or is discharged through an outlet pipe without the convergent-divergent nozzle. The desired end products are then separated from the gaseous stream.

대표청구항 ▼

The invention claimed is: 1. An apparatus for thermal conversion of one or more reactants to at least one desired end product, the apparatus comprising: an axial reactor having an inlet end, an outlet end, a reaction zone between the inlet end and the outlet end, and a reactor inlet at the inlet en

The invention claimed is: 1. An apparatus for thermal conversion of one or more reactants to at least one desired end product, the apparatus comprising: an axial reactor having an inlet end, an outlet end, a reaction zone between the inlet end and the outlet end, and a reactor inlet at the inlet end; a torch section configured to produce a heating gas; and an injector section interposed between the torch section and the axial reactor, the injector section including a heating gas inlet and at least one reactant inlet, the heating gas inlet and the at least one reactant inlet configured to provide all of the one or more reactants at a restricted diameter injection line within the injector section, the injector section being sized, located and configured to introduce one or more reactants into the heating gas and to promote substantially thorough mixing of the one or more reactants with the heating gas to produce a stream flowing axially toward the reactor inlet of the axial reactor, wherein the torch section, the injector section and the axial reactor are cooperatively configured such that any gas passing through the axial reactor enters the axial reactor through the inlet of the axial reactor. 2. The apparatus of claim 1, further comprising a convergent-divergent nozzle located coaxially with, and at an intended downstream location of, the outlet end of the axial reactor for rapidly cooling the gaseous stream by converting thermal energy to kinetic energy as a result of adiabatic and isentropic expansion as the stream flows axially through the nozzle. 3. The apparatus of claim 2, wherein the convergent-divergent nozzle has a converging section and a diverging section respectively leading to and from a restrictive open throat, the diverging section having a conical configuration centered along an axis of the axial reactor. 4. The apparatus of claim 2, further comprising a cooling section leading from the convergent-divergent nozzle. 5. The apparatus of claim 4, wherein the cooling section is configured to reduce the velocity of the stream while removing heat energy at a rate sufficient to prevent increases in its kinetic temperature and to retain the at least one desired end product within the stream. 6. The apparatus of claim 1, further comprising a cooling section in fluid communication with the outlet end of the axial reactor. 7. The apparatus of claim 6, wherein the cooling section is configured to reduce the velocity of the stream while removing heat energy at a rate sufficient to prevent increases in its kinetic temperature and to retain the desired end product within the stream. 8. The apparatus of claim 6, further comprising a converging section that connects the outlet end of the axial reactor to the cooling section. 9. The apparatus of claim 1, wherein the injector section comprises a multi-port injector located in an injector line. 10. The apparatus of claim 1, wherein the torch section includes an anode injector. 11. The apparatus of claim 1, further comprising an insulating layer surrounding the reaction zone. 12. The apparatus of claim 1, wherein the torch section comprises a plasma torch having a plasma arc inlet for introducing a stream of plasma arc gas to the plasma torch to produce a plasma. 13. The apparatus of claim 12, wherein the plasma torch includes at least one pair of electrodes positioned at an intended upstream location relative to the inlet end of the reactor. 14. The apparatus of claim 1, wherein the injector section comprises an injection line having a smaller diameter than a diameter of the reaction zone. 15. The apparatus of claim 11, wherein the insulating layer comprises a material selected from the group consisting of carbon, boron nitride, zirconia, silicon carbide, and combinations thereof. 16. The apparatus of claim 15, further comprising a cooling layer surrounding the insulating layer. 17. The apparatus of claim 1, further comprising a cooling section adjacent at least a portion of the reaction zone. 18. The apparatus of claim 17, wherein the cooling section is configured to circulate a liquid adjacent the at least a portion of the reaction zone.