Fuel nozzle having an inner tube and an outer tube engaged with the inner tube
US-9435262-B2 · Sep 6, 2016 · US
US12330940B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12330940-B2 |
| Application number | US-201917420940-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 19, 2019 |
| Priority date | Jan 31, 2019 |
| Publication date | Jun 17, 2025 |
| Grant date | Jun 17, 2025 |
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A process of partial oxidation is performed in a reactor which includes a reaction chamber and a burner assembly, wherein: the burner assembly has a single oxidant nozzle located within an fuel channel, said oxidant nozzle comprises a nozzle pipe and a nozzle outlet, the nozzle pipe and the fuel channel are arranged to produce a diffusion flame, the nozzle outlet has a shape with two or more elongate lobes projecting from a center of the nozzle pipe.
Opening claim text (preview).
What is claimed is: 1. A process for the production of synthesis gas containing hydrogen and carbon monoxide through a step of partial oxidation of a gaseous hydrocarbon fuel, wherein: said step of partial oxidation is performed in a reactor including a vessel, a reaction chamber and at least one burner assembly; said burner assembly has a single oxidant nozzle; said reactor includes at least one fuel channel which is in communication with an inlet of said gaseous hydrocarbon fuel; said oxidant nozzle comprises an oxidant nozzle pipe and an oxidant nozzle outlet, said oxidant nozzle pipe is coaxially arranged inside the fuel channel; the oxidant nozzle pipe and the fuel channel are arranged to produce a diffusion flame; the oxidant nozzle outlet has a shape with two or more elongate lobes projecting from an axis of the oxidant nozzle pipe; the process includes: feeding an oxidant in the oxidant nozzle of the reactor; feeding an hydrocarbon fuel in the fuel channel of the reactor, forming a diffusion flame at the outlet of the fuel nozzle. 2. The process according to claim 1 , wherein said oxidant nozzle outlet of the reactor has two elongate lobes symmetrically arranged opposite to each other. 3. The process according to claim 1 , wherein said oxidant nozzle outlet of the reactor has three or more elongate lobes which are radially arranged around the center of the oxidant nozzle pipe. 4. The process according to claim 3 , wherein the radially arranged elongate lobes of the reactor have a regular angular spacing. 5. The process according to claim 3 , wherein the number of radially arranged lobes of the reactor is two to eight. 6. The process according to claim 1 , wherein each elongate lobe of the reactor has two substantially parallel walls which merge at a distal tip of the lobe, and each elongate lobe has a radial length, from the center of the oxidant nozzle pipe to the distal tip, which is greater than the distance between said two parallel walls. 7. The process according to claim 6 , wherein the ratio (r/s) of said radial length over said distance between parallel walls is at least 2. 8. The process according to claim 1 , wherein the oxidant nozzle of the reactor has a transition region wherein the shape of the oxidant nozzle gradually changes from the shape of the nozzle pipe to the shape of nozzle outlet. 9. The process according to claim 1 , wherein the oxidant nozzle pipe of the reactor includes a portion with a cross section gradually decreasing towards the nozzle outlet. 10. The process according to claim 1 , wherein the oxidant nozzle and the fuel channel of the reactor are coaxial. 11. The process according to claim 1 , the burner assembly of the reactor being water-cooled or gas-cooled. 12. The process according to claim 1 , the burner of the reactor being made of any of: metal, a ceramic material, a composite ceramic material or a combination of these materials. 13. The process according to claim 1 , wherein said at least one burner assembly of the reactor is coupled to the vessel so that the oxidant nozzle of the burner assembly is at least partially accommodated within a fuel channel of the reactor. 14. The process according to claim 1 , wherein the reactor includes a plurality of burner assemblies fitted to the vessel and a plurality of fuel channels, wherein each of said burner assemblies has a respective oxidant nozzle and each oxidant nozzle is installed within a respective fuel channel and each of said fuel channels accommodate a single oxidant nozzle. 15. The process according to claim 1 , the reactor including at least one fuel channel which does not accommodate any oxygen nozzle. 16. The process according to claim 15 , the reactor including a single fuel channel and a plurality of burner assemblies arranged around said fuel channel. 17. The process according to claim 5 , wherein the number of radially arranged lobes of the reactor is three or four. 18. The process according to claim 7 , wherein the ratio (r/s) of said radial length over said distance between parallel walls is 2 to 40. 19. The process according to claim 7 , wherein the ratio (r/s) of said radial length over said distance between parallel walls is 5 to 20. 20. The process according to claim 1 , wherein the oxidant nozzle ends within the fuel channel, so that a lower part of said fuel channel makes an additional reaction chamber.
metallic · CPC title
ceramic · CPC title
characterised by surface shape · CPC title
of elongated shape, e.g. slits · CPC title
Methods of cooling · CPC title
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