Fixed bed or moving bed reactors with a radial flow of process stream to be treated, comprising improved internals
US-2018369774-A1 · Dec 27, 2018 · US
US9433910B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9433910-B2 |
| Application number | US-201214113958-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 27, 2012 |
| Priority date | May 3, 2011 |
| Publication date | Sep 6, 2016 |
| Grant date | Sep 6, 2016 |
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A module for a solid/heat-transfer gas reactor, including a plurality of diffusers each including a top portion supporting the solid reagent, and a portion for diffusing reactive/heat-transfer gas, situated under the top portion.
Opening claim text (preview).
The invention claimed is: 1. A solid/heat-transfer gas reactor comprising: a plurality of modules stacked in a vertical direction, comprising solid reagents configured to have the heat-transfer gas pass through them; wherein each module comprises a plurality of diffusers each including a top portion supporting one of the solid reagents, and a portion for diffusing reactive/heat-transfer gas, situated under the top support portion, and comprising a lateral gas-distribution channel, and a lateral gas-collection channel, each module further comprising a double wall between which the gas is configured to circulate before entering through the diffusers, the diffusers projecting upwards from a top wall of the double wall, and wherein any two directly consecutive modules in the stack define a housing cavity receiving one of the solid reagents carried at least partially by the diffusers arranged in the cavity, the lateral gas-distribution channels of the stacked modules forming together a vertical distributor supplying gas to each of spaces defined between two walls of the double walls, and wherein the lateral gas-collection channels of the stacked modules form together a vertical collector collecting the gas coming from each of the housing cavities. 2. A reactor according to claim 1 , wherein, in vertical projection onto a horizontal plane, the top portion supporting the solid reagents entirely covers the gas-diffusion portion. 3. A reactor according to claim 1 , wherein each diffuser takes a form of a cylindrical stud of which at least part of the lateral surface constitutes the gas-diffusion portion. 4. A reactor according to claim 1 , wherein, on each module, the diffusers are provided with a density of 75 to 150 diffusers/m 2 . 5. A reactor according to claim 1 , wherein each module is produced from three bent metal sheets fixed to one another, and by the diffusers. 6. A reactor according to claim 1 , further comprising means for bringing gas into the reactor, and means for discharging gas out of the reactor. 7. A solid/heat-transfer gas reaction method implemented by a reactor according to claim 6 , comprising: placing the solid reagents in each of the housing cavities; introducing the heat-transfer reactive gas into the distributor by gas-feed means; and after the gas passes through the solid reagents, the gas enters a collector of the reactor before being discharged from the collector by the gas-discharge means. 8. A method according to claim 7 , wherein the solid reagents are unstructured pure granular reagents. 9. A method according to claim 7 , wherein solid reagents of different natures are arranged in the housing cavities of the reactor.
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