Carbon dioxide separation using adsorption with steam regeneration
US-9504955-B2 · Nov 29, 2016 · US
US11097218B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11097218-B2 |
| Application number | US-201616346885-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 23, 2016 |
| Priority date | Nov 23, 2016 |
| Publication date | Aug 24, 2021 |
| Grant date | Aug 24, 2021 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Disclosed is a flue gas purification tower, comprising a tower body, at least one gas inlet (1) disposed at the bottom of the tower body, at least one gas outlet (2) disposed at the top of the tower body, at least one active coke layer (3) located inside the tower body, and a baffle plate (4) arranged in a place where the flow direction of the flue gas from the gas inlet changes. The baffle plate (4) is a straight plate, an arc plate, a straight-and-arc plate or a straight-arc-straight plate, wherein the straight-and-arc plate comprises a straight segment and an arc segment connected with each other; and the straight-arc-straight plate comprises a straight segment in the vertical direction, a straight segment in the horizontal direction, and an arc segment connected between the two straight segments.
Opening claim text (preview).
What is claimed is: 1. A flue gas purification tower, comprising a tower body, at least one gas inlet disposed at the bottom of the tower body, at least one gas outlet disposed at the top of the tower body, at least one active coke layer located inside the tower body, and a baffle plate arranged in a place where the flow direction of the flue gas from the gas inlet changes, wherein the baffle plate is formed with a plurality of circular holes or elongated holes. 2. The flue gas purification tower according to claim 1 , wherein the baffle plate is a straight plate, an arched plate, a straight-arched plate or a straight-arched-straight plate, wherein the straight-arched plate comprises a straight segment and an arched segment connected with each other; and the straight-arched-straight plate comprises a straight segment in the vertical direction, a straight segment in the horizontal direction, and an arched segment connected between the two straight segments. 3. The flue gas purification tower according to claim 2 , wherein all the arched plate, the arched segment of the straight-arched plate and the arched segment of the straight-arched-straight plate have a radius between 1 m and 3 m. 4. The flue gas purification tower according to claim 1 , wherein the number of the baffle plate is 3-5. 5. The flue gas purification tower according to claim 1 , wherein the baffle plate has the same length as the gas inlet and a height between 1 m and 3 m. 6. The flue gas purification tower according to claim 1 , wherein the active coke layer has a thickness between 1.4 m and 1.9 m. 7. The flue gas purification tower according to claim 1 , wherein the tower body has a length between 6 m and 10 m, a width between 6 m and 10 m and a height between 20 m and 40 m.
according to the "moving bed" method · CPC title
Means for feeding or distributing gases · CPC title
Ammonia · CPC title
Beds in columns · CPC title
Nitrogen oxides other than dinitrogen oxide · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.