Method and apparatus for pre-heating recirculated flue gas to a dry scrubber during periods of low temperature
US-9186625-B2 · Nov 17, 2015 · US
US9901869B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9901869-B2 |
| Application number | US-201615231899-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 9, 2016 |
| Priority date | Oct 7, 2011 |
| Publication date | Feb 27, 2018 |
| Grant date | Feb 27, 2018 |
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 wet scrubber for cleaning a process gas containing sulphur dioxide comprises an absorption vessel for contacting the process gas with an absorption liquid to absorb sulphur dioxide from the process gas, a sensor for measuring a concentration in the absorption liquid, and a control unit. The control unit is adapted to receive a measurement signal from the sensor and to control, based on the measured concentration, at least one wet scrubber operating parameter influencing the concentration in the absorption liquid.
Opening claim text (preview).
The invention claimed is: 1. A method of controlling a wet scrubber used to clean a process gas containing sulphur dioxide, the method comprising: contacting the process gas with an absorption liquid in an absorption vessel to absorb sulphur dioxide from the process gas; measuring a concentration of sulphite in the absorption liquid to obtain a sulphite concentration measurement; and controlling, based on the sulphite concentration measurement as compared to a set point therefor, at least one scrubber operating parameter influencing the concentration of sulphite in the absorption liquid, by effecting, when the sulphite concentration measurement exceeds the set point, a reduction of a pH of the absorption liquid accompanied by at least one of: increasing a liquid to gas ratio in the absorption vessel; and increasing a supply of an absorption enhancing additive to the absorption liquid. 2. The method according to claim 1 , further comprising: effecting, when the sulphite concentration measurement exceeds the set point, at least one of: increasing a supply of a gas containing oxygen to the absorption liquid; supplying an absorption enhancing additive to the absorption liquid. 3. The method according to claim 1 , further comprising: effecting, when the sulphite concentration measurement is below the set point, at least one of: reducing a supply of a gas containing oxygen to the absorption liquid; increasing a pH of the absorption liquid; and reducing a supply of an absorption enhancing additive to the absorption liquid. 4. The method according to claim 1 , further comprising: effecting, when the sulphite concentration measurement is below the set point, an increase of a pH of the absorption liquid accompanied by at least one of: reducing a liquid to gas ratio in the absorption vessel; and reducing a supply of an absorption enhancing additive to the absorption liquid. 5. The method according to claim 1 , further comprising: collecting absorption liquid after sulphur dioxide absorption by the absorption liquid from the process gas; and measuring a sulphite concentration of the collected absorption liquid to obtain a sulphite concentration measurement prior to mixing the absorption liquid with absorbent material. 6. The method according to claim 1 , further comprising: collecting absorption liquid after sulphur dioxide absorption by the absorption liquid from the process gas; and measuring a sulphite concentration of the collected absorption liquid to obtain a sulphite concentration measurement prior to mixing the absorption liquid with absorbent material and prior to bubbling an oxygen containing gas through the absorption liquid. 7. The method according to claim 1 , further comprising: collecting absorption liquid after sulphur dioxide absorption by the absorption liquid from the process gas; and measuring the concentration of sulphite within 1 minute of collecting the absorption liquid from the absorption vessel. 8. The method according to claim 1 , further comprising: collecting absorption liquid after sulphur dioxide absorption by the absorption liquid from the process gas and prior to bubbling an oxygen containing gas through the absorption liquid; measuring a first concentration of sulphite of the collected absorption liquid to obtain a first measurement; collecting absorption liquid after the absorption liquid is exposed to a bubbling of oxygen containing gas; measuring a second concentration of sulphite of the exposed absorption liquid to obtain a second measurement, and comparing the first measurement to the second measurement to determine whether the concentration of sulphite is increasing or decreasing. 9. The method according to claim 1 , further comprising: detecting, based on a comparison between a first sulphite concentration measurement and a second sulphite concentration measurement, if the sulphite concentration of the absorption liquid is increasing; and effecting, when the sulphite concentration is increasing, at least one of: increasing a supply of a gas containing oxygen to the absorption liquid; reducing a pH of the absorption liquid; and supplying an absorption enhancing additive to the absorption liquid.
Mercury or mercury compounds · CPC title
Activators, promoting agents, catalytic agents or enzymes · CPC title
Hydrofluoric acid · CPC title
with gas-liquid contact · CPC title
Removing sulfur dioxide or sulfur trioxide · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.