Rate/kinetic selective multiple bed adsorption process cycle
US-11883775-B2 · Jan 30, 2024 · US
US9844753B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9844753-B2 |
| Application number | US-201314416917-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 3, 2013 |
| Priority date | Jul 25, 2012 |
| Publication date | Dec 19, 2017 |
| Grant date | Dec 19, 2017 |
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A plant for purifying a gas stream comprising at least 0.02% by volume of water, CO 2 and NOx, comprising an adsorber characterized by: a cavity ( 1 ); an adsorbent ( 2 ) included in the cavity ( 1 ); an outer casing ( 3 ) made of carbon steel; an inner casing ( 4 ) made of stainless steel making a space having a width of between 10 and 100 mm between said inner casing and the outer casing, said space being at equal pressure with the cavity.
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The invention claimed is: 1. A process for purifying a gas stream comprising, CO 2 , NOx, and at least 0.02% by volume of water, comprising using an adsorber, wherein said adsorber comprises: a cavity; an adsorbent included within the cavity; an outer casing made of carbon steel; an inner casing made of stainless steel, wherein a space between 10 and 100 mm wide is between said inner casing and the outer casing, said space being at equal pressure with the cavity, the process comprising subjecting the adsorber to a purification cycle comprising an adsorption step and a regeneration step using a regeneration gas and wherein nitric acid and liquid water are present in the adsorber during the regeneration step. 2. The process as claimed in claim 1 , wherein the adsorber further comprises a separator pot, and wherein the nitric acid and the liquid water are removed from the adsorber via the separator pot. 3. The process of claim 1 , wherein the regeneration step is carried out at a temperature above 150° C. 4. An apparatus for purifying a gas stream comprising CO 2 , NOx, and at least 0.02% by volume of water, comprising an adsorber, wherein said adsorber comprises: a cavity; an adsorbent included within the cavity; an outer casing made of carbon steel; an inner casing made of stainless steel, wherein a space between 10 and 100 mm wide is between said inner casing and the outer casing, said space being at equal pressure with the cavity. 5. The apparatus in claim 4 , wherein the space is at equal pressure with the cavity by means of a gas connection that opens into the cavity downstream of the adsorbent when considering the path of the gas stream. 6. The apparatus in claim 4 , wherein the inner casing is divided into at least two inner casings that form a double casing. 7. The apparatus in claim 6 , wherein, among the two inner casings, only the innermost inner casing of the adsorber is made of stainless steel. 8. The apparatus in claim 4 , further comprising; the outer casing divided into a shell, a first base on the inlet side of the gas stream and a second base on the outlet side of the gas stream, and the inner casing is present level with the shell and continues over the first base. 9. The apparatus in claim 4 , further comprising; the outer casing divided into a shell, a first base on the inlet side of the gas stream and a second base on the outlet side of the gas stream, the inner casing is present level with said shell, and a stainless steel plate is plated on the first base. 10. The apparatus of claim 8 , further comprising: said adsorber comprises a separation pot integrated into or joined to the first base that makes it possible to separate acid condensates from a gas leaving on the inlet side of the gas stream to be purified and an outlet pipe for discharging said gas stripped of its condensates. 11. The apparatus of claim 4 , wherein the adsorber comprises silica gel as adsorbent.
Nitrogen oxides other than dinitrogen oxide · CPC title
Carbon dioxide · CPC title
Silica or silicates · CPC title
Flue gases · CPC title
Carbon oxides · CPC title
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