Carbon dioxide separation using adsorption with steam regeneration
US-9504955-B2 · Nov 29, 2016 · US
US9513068B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9513068-B2 |
| Application number | US-201214123524-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 7, 2012 |
| Priority date | Jun 7, 2011 |
| Publication date | Dec 6, 2016 |
| Grant date | Dec 6, 2016 |
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A solid/heat-transport and reactive gas reactor, including: a helical duct including an inlet and an outlet, the helical duct defining a helical bottom track on which a solid reagent can slide from the inlet to the outlet of the helical duct; a mechanism for bringing the solid reagent to the inlet of the helical duct; a mechanism for causing a heat-transport gas to flow in the helical duct, from the outlet to the inlet of the helical duct; a reservoir of solid reagent under the outlet of the helical duct; and a conveyor for conveying the reagent from a low point of the reservoir to the bringing mechanism.
Opening claim text (preview).
The invention claimed is: 1. A solid/heat-transport and reactive gas reactor, comprising: a helical duct including a first tube shaped as a helix and having an inlet and an outlet, the helical duct defining a helical bottom track on which a solid reagent can slide from the inlet to the outlet of the helical duct; an opening configured to bring the solid reagent to the inlet of the helical duct; means for causing a heat-transport gas to flow in the helical duct, from the outlet to the inlet of the helical duct; a second tube shaped as a helix, wherein the first tube is disposed in the second tube and defines a space between both of the first tube and the second tube, and wherein the space between the first tube and the second tube is configured to have a heat-transport fluid pass through the space, so that heat exchange can occur between the heat-transport gas circulating in the first tube and the heat-transport fluid, a reservoir of solid reagent under the outlet of the helical duct; and a conveyor configured to convey the solid reagent from a low point of the reservoir to the opening configured to bring the solid reagent to the inlet of the helical duct. 2. The reactor according to claim 1 , wherein the helical duct comprises a plurality of passages each emerging on either side of the helical bottom track, at a given turn on the helical duct, and in a directly lower turn of the helical duct. 3. The reactor according to claim 1 , wherein the helical duct is configured so that the solid reagent slides by gravity over the helical bottom track. 4. The reactor according to claim 1 , further comprising a vibrator configured to vibrate the helical duct to make the solid reagent slide over the helical bottom track. 5. The reactor according to claim 1 , further comprising a heat exchanger supplied by the heat-transport gas coming from the inlet of the helical duct. 6. The reactor according to claim 1 , wherein the helical duct has a vertical axis. 7. A solid/heat-transport gas method implemented by a reactor according to claim 1 , comprising: sliding the solid reagent over the helical bottom track from the inlet to the outlet of the helical duct; and making the heat-transport gas flow in an opposite direction in the helical duct from the outlet to the inlet of the helical duct. 8. The method according to claim 7 , wherein the solid reagent is a powder.
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