NOx removal from gaseous effluents

Patent metadata

Field	Value
Publication number	US-12410108-B2
Application number	US-201917045165-A
Country	US
Kind code	B2
Filing date	Apr 5, 2019
Priority date	Apr 6, 2018
Publication date	Sep 9, 2025
Grant date	Sep 9, 2025

Abstract

The present application relates to a process for the reduction of NOx from a gaseous effluent generated in the production of fertilizer comprising the acid digestion of phosphate ore in the presence of urea, wherein said gaseous effluent generated has a NOx composition of 70 to 100 mole % NO 2 and 0 to 30 mole % NO, comprising the steps of: a) contacting said gaseous effluent for 0.5 to 15 seconds with ozone, thereby providing a resultant gas mixture wherein NO and NO 2 present in the NOx are oxidized to higher nitrogen oxides; and; b) removing higher nitrogen oxides from said resultant gas mixture; wherein urea is present during said acid digestion of phosphate ore in an amount of 0.25 wt % or less based on the weight of said phosphate ore; and; ozone is added to said gaseous effluent in an ozone/NOx ratio ranging between 0.5 and 1.4.

First claim

The invention claimed is:

1. A process for the reduction of mono-nitrogen oxides (NOx) from a gaseous effluent generated in the production of fertilizer comprising the acid digestion of phosphate ore in the presence of urea, wherein said gaseous effluent generated has a NOx composition of 70 to 100 mole % NO 2 and 0 to 30 mole % NO, comprising the steps of:
a) contacting said gaseous effluent for 0.5 to 15 seconds with ozone, thereby providing a resultant gas mixture wherein NO and NO 2 present in the NOx are oxidized to higher nitrogen oxides; and;
b) removing higher nitrogen oxides from said resultant gas mixture;
wherein urea is added during said acid digestion of phosphate ore in an amount between 0.001 wt % and 0.25 wt % based on the weight of said phosphate ore; and;
ozone is added to said gaseous effluent in an ozone/NOx ratio ranging between 0.5 and 1.4,
wherein the resultant gas mixture has an NOx level of 20 to 80 ppm and an N 2 O level of less than 15 ppm.

2. The process according to claim 1 , wherein step b) is performed using a wet scrubber.

3. The process according to claim 2 , wherein said wet scrubber an aqueous acidic scrubber.

4. The process according to claim 1 , wherein said higher nitrogen oxide comprises N 2 O 5 .

5. The process according to claim 1 , wherein said gaseous effluent comprises sulphur oxides, water vapour, hydrogen fluoride, silicon tetrafluoride, nitric acid and/or carbon dioxide dust.

6. The process according to claim 1 , wherein the scrubber in step b) is the only scrubber used for the removal of NOx from said gaseous effluent.

7. The process according to claim 1 , wherein nitric acid or a salt thereof is formed in step b).

8. The process according to claim 1 , wherein the temperature in step a) is at most 130° C.

9. The process according to claim 1 , wherein a gas analyser measures the concentration of NOx in the gaseous effluent and regulates the amount of ozone added to the gaseous effluent in step a) on the basis of the NOx concentration measured.

10. The process according to claim 1 wherein urea is added during said acid digestion of phosphate ore in an amount between 0.005 wt % and 0.08 wt %, based on the weight of said phosphate ore.

11. A process for the reduction of mono-nitrogen oxides (NOx) from a gaseous effluent generated in the production of fertilizer comprising the acid digestion of phosphate ore in the presence of urea, wherein said gaseous effluent generated has a NOx composition of 70 to 100 mole % NO 2 and 0 to 30 mole % NO, comprising the steps of:
a) contacting said gaseous effluent for 0.5 to 15 seconds with ozone, thereby providing a resultant gas mixture wherein NO and NO 2 present in the NOx are oxidized to higher nitrogen oxides; and;
b) removing higher nitrogen oxides from said resultant gas mixture;
wherein urea is added during said acid digestion of phosphate ore in an amount between 0.005 wt % and 0.07 wt % based on the weight of said phosphate ore; and;
ozone is added to said gaseous effluent in an ozone/NOx ratio ranging between 0.5 and 1.4, and wherein the resultant gas mixture has a NOx level of less than 90 ppm and an N 2 O level of less than 15 ppm.

12. The process of claim 11 wherein the urea is added in an amount between 0.02 to 0.06 wt %.

13. The process of claim 12 wherein the urea is added in an amount between 0.02 to 0.05 wt %.

14. A process for the removal of mono-nitrogen oxides (NOx) from gaseous effluents in the production of fertilizer, the process comprising digesting phosphate ore with acid, thereby forming a digesting mixture and gaseous effluents; adding urea to the digesting mixture; and adding ozone to the gaseous effluents, wherein the gaseous effluents generated in the production of fertilizer have a NOx composition of 70 to 100 mole % NO 2 and 0 to 30 mole % NO, and wherein urea is added in the digesting mixture in an amount between 0.001 wt % and 0.07 wt % based on the weight of said phosphate ore.

15. The process according to claim 14 , wherein ozone is used in a molar ratio of ozone over NOx in the gaseous effluent of 0.5 to 1.4.

Assignees

• Yara Int Asa

Inventors

• Louwe Robertus
• Kita Patrycja
• Sund Lene

Classifications

• C05B11/08

  using sulfuric acid · CPC title

• C05B11/04

  using mineral acid · CPC title

• B01D11/04

  of solutions which are liquid · CPC title

• B01D53/78

  with gas-liquid contact · CPC title

• B01D53/76

  Gas phase processes, e.g. by using aerosols · CPC title