System and Process For Removal Of Organic Carboxylates From Mono Ethylene Glycol (MEG) Water Streams By Acidification and Vaporization Under Vacuum
US-2015104356-A1 · Apr 16, 2015 · US
US10144686B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10144686-B2 |
| Application number | US-201715675260-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 11, 2017 |
| Priority date | Apr 1, 2016 |
| Publication date | Dec 4, 2018 |
| Grant date | Dec 4, 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 system and method for removing acetic acid and other short chain fatty acids described as organic acid from a rich mono-ethylene glycol (“MEG”) solution does so by stripping the organic acid from the rich MEG solution by contacting the solution with a gas, the gas being nitrogen or a fuel gas such as methane; and stripping the organic acid from the gas by contacting the gas with a caustic solution such as a dilute sodium hydroxide solution. The stripping steps take place in respective stripping columns. A portion of the gas exiting the gas/organic acid stripping column can be recycled to the MEG/organic acid stripping column to reduce total gas usage. A portion of the waste stream exiting the gas/organic acid stripping column can be recycled back to the gas/organic acid stripping column to reduce the amount of caustic solution used as well as the amount of waste.
Opening claim text (preview).
What is claimed: 1. A method for removing organic acid from a MEG stream, the method comprising: stripping the organic acid from the MEG stream after a hydrate inhibition use of the MEG stream by contacting the MEG stream with a gas wherein the MEG stream after the contact with the gas is substantially free of the organic acid. 2. A method according to claim 1 further comprising: washing the organic acid contained in the gas that contacted the MEG stream by contacting the gas with a caustic solution wherein the gas after the contact with the caustic solution is substantially free of the organic acid. 3. A method according to claim 2 further comprising recycling a portion of the gas for use in the stripping of the organic acid from the MEG stream. 4. A method according to claim 2 further comprising recycling a portion of a waste stream from the washing of the organic acid contained in the gas for use in the washing of the organic acid contained in the gas. 5. A method according to claim 2 wherein the caustic solution is a sodium hydroxide solution comprising about 1% sodium hydroxide. 6. A method according to claim 1 further comprising adjusting, when needed, a pH of the MEG stream to a pH<4. 7. A method for removing organic acid from a MEG stream, the method comprising the steps of: stripping the organic acid from the MEG stream after a hydrate inhibition use of the MEG stream by contacting the MEG stream with a gas wherein the MEG stream after the contact with the gas is substantially free of the organic acid; and washing the organic acid contained in the gas that contacted the MEG stream by contacting the gas with a caustic solution, wherein the gas after contact by the caustic solution is substantially free of the organic acid. 8. A method according to claim 7 wherein the organic acid is a carboxylic acid. 9. A method according to claim 7 further comprising recycling a portion of the gas for use in the stripping of the organic acid from the MEG stream. 10. A method according to claim 7 further comprising recycling a portion of a waste stream from the washing of the organic acid contained in the gas for use in the washing of the organic acid contained in the gas. 11. A method according to claim 7 wherein the caustic solution is a sodium hydroxide solution comprising about 1% sodium hydroxide. 12. A method according to claim 7 further comprising the step of adjusting, when needed, a pH of the MEG stream to a pH<4. 13. A MEG reclamation and regeneration system the system comprising a MEG/organic acid stripping column; and a gas/organic acid washing column; the MEG/organic acid stripping column configured to receive a stripping gas and a MEG stream containing the organic acid, the MEG stream exiting the MEG/organic stripping column as a substantially organic acid-free rich MEG stream; the stripping gas including the organic acid exiting the MEG/organic stripping column; and the gas/organic acid washing column configured to receive a caustic solution and the stripping gas including the organic acid exiting the MEG/organic stripping column, the gas exiting the gas/organic washing column as a substantially organic acid free gas stream. 14. A system according to claim 13 further comprising a recycle loop, the recycle loop configured to receive a portion of the substantially organic acid gas free stream exiting the gas/organic acid washing column and route the portion back to the MEG/organic stripping column. 15. A system according to claim 13 further comprising a recycle loop, the recycle loop configured to receive a portion of a waste stream exiting the gas/organic acid washing column and route the portion back to the gas/organic acid washing column. 16. A system according to claim 13 , the stripping gas being nitrogen. 17. A system according to claim 13 , the stripping gas being methane. 18. A MEG regeneration and reclamation system comprising: a MEG/organic acid stripping column; and a gas/organic acid washing column; the MEG/organic acid stripping column configured to receive a stripping gas and a MEG stream containing an organic acid; the MEG stream exiting the MEG/organic stripping column as a substantially organic acid-free MEG stream; the gas/organic acid washing column arranged to receive a caustic solution and the stripping gas containing the organic acid exiting the MEG/organic stripping column, the stripping gas exiting the gas/organic washing column as a substantially organic acid-free gas stream; wherein a pH of the MEG stream is less than 4; and wherein the stripping gas is selected from the group consisting of nitrogen and methane. 19. A system according to claim 18 , the stripping gas being selected from a group consisting of nitrogen and methane. 20. A system according to claim 18 further comprising a first and a second recycle loop, the first recycle loop configured to receive a portion of the substantially organic acid gas free stream exiting the gas/organic acid washing column and route the portion back to the MEG/organic stripping column; the second recycle loop configured to receive a portion of a waste stream exiting the gas/organic acid washing column and route the portion back to the gas/organic acid washing column.
with gas-liquid contact · CPC title
by conversion of the acids, their salts, esters or anhydrides with the same carboxylic acid part · CPC title
Limiting or prohibiting hydrate formation · CPC title
the substance being a gas · CPC title
by physical treatment · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.