Production of Higher Alcohols with Minimum Methanol Content from the Gasification of Carbonaceous Materials
US-2015361015-A1 · Dec 17, 2015 · US
US9777232B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9777232-B2 |
| Application number | US-201414762525-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 22, 2014 |
| Priority date | Feb 21, 2013 |
| Publication date | Oct 3, 2017 |
| Grant date | Oct 3, 2017 |
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.
The system includes: an absorber which brings an introduction gas into contact with an absorbent that absorbs CO 2 and H 2 S; an absorbent regenerator which releases CO 2 or the like to regenerate the absorbent; a second supply line which returns a regenerated absorbent to the absorber from the regenerator; a third supply line which extracts a semi-rich solution from the vicinity of a middle stage of the absorber, and introduces the semi-rich solution to the vicinity of the middle stage of the regenerator; and a semi-rich solution heat exchanger which is interposed at an intersection between the third supply line and the second supply line to perform the heat exchange between the semi-rich solution and the lean solution.
Opening claim text (preview).
The invention claimed is: 1. A method for recovering a gas containing CO2 and H2S using an absorber and a regenerator, the method comprising: extracting a semi-rich solution which has absorbed a part of CO2 and H2S contained in an introduction gas from the vicinity of a middle stage of the absorber to be introduced into the vicinity of a middle stage of the regenerator; extracting a rich solution which has absorbed CO2 and H2S contained in the introduction gas from a bottom portion of the absorber to be introduced into the vicinity of a top portion of the regenerator; separating a non-condensable gas including N2, H2 and CO contained in the semi-rich solution in a first flash drum prior to introduction into the vicinity of the middle stage of the regenerator, and separating a non-condensable gas including N2, H2 and CO contained in the rich solution in a second flash drum prior to introduction into the vicinity of the top portion of the regenerator; heat-exchanging the semi-rich solution with a lean solution regenerated by removing CO2 and H2S contained in the semi-rich solution and the rich solution in the regenerator; cooling water vapor accompanied by CO2 and H2S gas released from the regenerator with a condenser to condense the water vapor into water; separating the water and the CO2 and H2S gas in a separation drum; and joining the CO2 and H2S separated in the separation drum and the non-condensable gas separated in the first and second flash drums.
Hydrogen sulfide · CPC title
Selection of liquid materials for use as absorbents · CPC title
Cross-Sectional Technologies · mapped topic
Regeneration of liquid absorbents · CPC title
Sulfur containing contaminants, e.g. hydrogen sulfide · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.