Method for removing acid gases from a fluid flow containing nitrogen oxides

Patent metadata

Field	Value
Publication number	US-2016166975-A1
Application number	US-201414902670-A
Country	US
Kind code	A1
Filing date	Jul 4, 2014
Priority date	Jul 5, 2013
Publication date	Jun 16, 2016
Grant date	—

Abstract

A process for separating off acid gases from a nitrogen oxide-comprising fluid stream, wherein a) the fluid stream is brought into contact in an absorption zone with an aqueous absorbent which comprises at least one amino group-comprising compound, wherein a deacidified fluid stream is obtained, b) the deacidified fluid stream is brought into contact in at least one scrubbing zone with an aqueous scrubbing liquid and a de-aminated deacidified fluid stream is obtained, wherein the scrubbing liquid is recycled via at least one scrubbing zone, c) overflow from the at least one scrubbing zone is treated with UV light, and d) the UV-treated overflow is combined with the absorbent. The process permits the efficient degradation of the nitrosamines present in the absorbent.

First claim

1 . A process for separating off-acid gases from a fluid stream that includes nitrogen oxide the process comprising;
a) contacting the fluid stream in an absorption zone with an aqueous absorbent that includes at least one amino group-comprising compound to provide a deacidified fluid stream, b) contacting the deacidified fluid stream in at least one scrubbing zone with an aqueous scrubbing liquid and a de-aminated, deacidified fluid stream, wherein the scrubbing liquid is recycled via at least one scrubbing zone, c) treating overflow from the at least one scrubbing zone with UV light, and d) combining the UV-treated overflow with the aqueous absorbent.

2 . The process according to claim 1 , wherein the contacting of the deacidified fluid stream with an aqueous scrubbing liquid is conducted in a cascade of scrubbing zones.

3 . The process according to claim 2 , wherein the deacidified fluid stream is conducted through a first scrubbing zone and then conducted through a second scrubbing zone, wherein aqueous scrubbing liquid is recycled via the second scrubbing zone, overflow from the second scrubbing zone is conducted through the first scrubbing zone without recycling and overflow from the first scrubbing zone is treated with UV light.

4 . The process according to claim 2 , wherein the deacidified fluid stream is conducted through a first scrubbing zone and then conducted through a second scrubbing zone, wherein aqueous scrubbing liquid is recycled via each scrubbing zone, overflow from the second scrubbing zone is passed into the first scrubbing zone and overflow from the first scrubbing zone is treated with UV light.

5 . The process according to claim 2 , wherein a recycling ratio of the scrubbing zone situated furthest upstream with respect to the direction of flow of the deacidified fluid stream is 5 to 100.

6 . The process according to claim 1 , wherein a ratio of the intensity of the UV light in the wavelength range from 220 to 380 nm to the intensity of the UV light in the wavelength range from 100 to 380 nm is at least 0.85.

7 . The process according to claim 1 , wherein the absorption zone is arranged in an absorption column and the at least one scrubbing zone is constructed as a section of the absorption column arranged above the absorption zone.

8 . The process according to claim 2 , further comprising passing feed water into the last scrubbing zone.

9 . The process according to claim 8 , wherein the feed water comprises at least in part freshwater.

10 . The process according to claim 9 , wherein the amount of freshwater substantially corresponds to the amount of water loss of the absorbent circuit.

11 .- 13 . (canceled)

14 . The process according to claim 1 , wherein the absorbent comprises at least one amine which comprises at least one secondary amino group.

15 . The process according to claim 1 , wherein the fluid stream is a flue gas stream.

16 . The process according to claim 2 , wherein the aqueous absorbent loaded with acid gases is regenerated in a desorption zone by heating with partial evaporation of the absorbent, wherein the acid gases are at least in part liberated.

17 . The process according to claim 16 , further comprising cooling the liberated acid gases to condense at least in-part entrained steam, and the condensate is passed at least in part as feed water to the last scrubbing zone.

18 . The process according to claim 1 , further comprising scrubbing the de-aminated, deacidified fluid stream with an acidic aqueous solution.

Assignees

• Basf Se

Inventors

• Sieder Georg
• Clausen Iven
• Garcia Palacios Javier
• Lozano Martinez Gustavo Adolfo

Classifications

• B01D53/1456

  Removing acid components · CPC title

• B01D53/1425 Primary

  Regeneration of liquid absorbents · CPC title

• B01D2252/204

  Amines · CPC title

• B01D2258/0283

  Flue gases · CPC title

• B01D2257/404

  Nitrogen oxides other than dinitrogen oxide · CPC title