Method and apparatus for sustainable carbon dioxide sequestration
US-2024424442-A1 · Dec 26, 2024 · US
US10940431B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10940431-B2 |
| Application number | US-201916580306-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 24, 2019 |
| Priority date | Jan 17, 2014 |
| Publication date | Mar 9, 2021 |
| Grant date | Mar 9, 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.
A reclaiming method is disclosed including conducting evaporation by introducing a part of the absorbent to recover CO2 or H2S in a gas in a closed system recovery unit and separating a degraded substance contained in the absorbent from the absorbent to be introduced into an evaporator and obtain recovery steam containing an absorbent and CO2 or H2S by a heating section that is provided on a circulation line that circulates in the evaporator; and removing ionic degraded substance by cooling the concentrate obtained in the evaporation and removing an ionic degraded substance in the concentrate after the cooling, wherein a purified concentrate from which the ionic degraded substance has been removed is reused as a purified absorbent.
Opening claim text (preview).
The invention claimed is: 1. A reclaiming method comprising: conducting evaporation by introducing a part of an absorbent to recover CO 2 or H 2 S in a gas in a recovery unit into an evaporator and heating and concentrating the part of the absorbent to obtain recovery steam containing the absorbent and CO 2 or H 2 S and concentrate; discharging the recovery steam from a top of the evaporator; drawing off and supplying the concentrate from a bottom side of the evaporator; removing an ionic degraded substance by cooling the concentrate supplied from the evaporator and removing the ionic degraded substance contained in the concentrate after the cooling to obtain a purified concentrate; and reusing purified concentrate as a purified absorbent in the recovery unit. 2. The reclaiming method according to claim 1 , wherein in the removing the ionic degraded substance, electrodialysis or an ion exchange resin is used. 3. The reclaiming method according to claim 2 , wherein, in the removing the ionic degraded substance, the ion exchange resin is used, the ion exchange resin is regenerated by introducing a regenerating chemical into the ion exchange resin and concentrating a resin-regenerated waste liquid obtained by regenerating the ion exchange resin with the introduced chemical on the evaporator side. 4. The reclaiming method according to claim 1 , comprising irradiating an ultraviolet light to decompose a nonionic degraded substance contained in the concentrate after removing the ionic degraded substance.
Irradiation devices or lamp constructions · CPC title
Ion-exchange processes in general; Apparatus therefor (ion-exchange chromatography processes or apparatus B01D15/08) · CPC title
by ion-exchange (ion-exchange in general B01J) · CPC title
Purification of waste water by evaporation · CPC title
Removing mixtures of hydrogen sulfide and carbon dioxide · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.