Catalyst support systems for ammonia oxidation burners
US-2020338518-A1 · Oct 29, 2020 · US
US9242216B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9242216-B2 |
| Application number | US-201214343696-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 7, 2012 |
| Priority date | Sep 9, 2011 |
| Publication date | Jan 26, 2016 |
| Grant date | Jan 26, 2016 |
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Burner basket system for ammonia oxidation burners for industrial plants with burner diameters of 2-7 m in a natural- or forced-circulation boiler suitable for minimizing gas slip and for minimizing wave formation contents in the burner basket and loss of contents in the burner basket, wherein the burner basket has a wall anchored in the ammonia oxidation burner and the burner basket has a gas-permeable bottom plate, placed on internal fittings of the forced circulation boiler, wherein the wall and the gas-permeable bottom plate are not mechanically connected to each other, and the wall of the burner basket tapers conically towards the bottom plate at an angle of 5-20° from the perpendicular, and in all operating states of the ammonia oxidation burner there is a peripheral gap in the range from 5 to 10 mm between the wall and the gas-permeable bottom plate.
Opening claim text (preview).
The invention claimed is: 1. A system of a burner basket for ammonia oxidation burners for commercial-scale plants with burner diameters of 2-7 m in a natural or forced circulation boiler, the system being suited to minimize gas slip and to minimize surface corrugation of media contained in the burner basket as well as to minimize loss of media contained in the burner basket, with the burner basket being provided with a wall which is fixed to the ammonia oxidation burner, and the burner basket being provided with a gas-permeable bottom plate arranged on top of internal components of the natural or forced circulation boiler, the wall and the gas-permeable bottom plate not being connected mechanically, and the wall of the burner basket being tapered conically towards the bottom plate at an angle of 5-20° relative to vertical and a circumferential gap in the range of 5 to 10 mm being produced between the wall and the gas-permeable bottom plate under all operating conditions of the ammonia oxidation burner. 2. The system of a burner basket for ammonia oxidation burners for commercial-scale plants with burner diameters of 2-7 m in a natural or forced circulation boiler according to claim 1 , wherein there is an additional gas-permeable structure on top of the gas-permeable bottom plate. 3. The system of a burner basket for ammonia oxidation burners for commercial-scale plants with burner diameters of 2-7 m in a natural or forced circulation boiler according to claim 2 , wherein the additional gas-permeable structure extends over the gap between the wall and the gas-permeable bottom plate. 4. The system of a burner basket for The system of a burner basket for ammonia oxidation burners for commercial-scale plants with burner diameters of 2-7 m in a natural or forced circulation boiler according to claim 2 , wherein the additional gas-permeable structure is of a smaller mesh size than the gas-permeable bottom plate. 5. The system of a burner basket for ammonia oxidation burners for commercial-scale plants with burner diameters of 2-7 m in a natural or forced circulation boiler according to claim 1 , wherein the gas-permeable bottom plate is a honeycomb-structured grid, a mesh plate, a sieve plate, a grid plate or a perforated plate. 6. A method for minimizing gas slip and for minimizing surface corrugation of media contained in the burner basket as well as for minimizing the loss of media contained in the burner basket of an ammonia oxidation burner for commercial-scale plants with burner diameters of 2-7 m, comprising the step of: providing a natural or forced circulation boiler, wherein the burner basket is provided with a wall which is fixed to the ammonia oxidation burner, and the burner basket is provided with a gas-permeable bottom plate arranged on top of internal components of the natural or forced circulation boiler, the wall and the gas-permeable bottom plate not being connected mechanically and a circumferential gap being produced between gas-permeable bottom plate and wall, and wherein the wall of the burner basket is tapered conically towards the bottom plate at an angle of 5-20° relative to vertical, with the width of the gap enlarging to a maximum of 10 mm during operation of the ammonia oxidation burner. 7. The method according to claim 6 , wherein an additional gas-permeable fabric is arranged on top of the gas-permeable bottom plate to improve the sealing effect, the fabric extending over the gap and being of a smaller mesh size than the gas-permeable bottom plate.
Apparatus · CPC title
Means for preventing deterioration or loss of catalyst or for recovering lost catalyst · CPC title
in a cylindrical annular shaped bed · CPC title
Construction aspects · CPC title
Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction (B01J8/0285, B01J8/067, B01J8/087, B01J8/1836 take precedence) · CPC title
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