Method for producing a sncr/scr solution

Patent metadata

Field	Value
Publication number	US-2025084032-A1
Application number	US-202218682550-A
Country	US
Kind code	A1
Filing date	Aug 26, 2022
Priority date	Aug 26, 2021
Publication date	Mar 13, 2025
Grant date	—

Abstract

A method for producing a SNCR/SCR solution, comprising the steps of: a) reacting ammonia and carbon dioxide in a high pressure section, thereby obtaining an aqueous composition comprising urea and ammonium salts; b) processing the aqueous composition obtained in step a), thereby obtaining a first aqueous solution comprising urea, and a second aqueous solution comprising ammonium salts; and c) diluting the second aqueous solution comprising ammonium salts obtained in step b) with a third aqueous solution, thereby producing the SNCR/SCR solution. The present disclosure also provides the use of an aqueous stream comprising ammonium salts from a urea-producing plant for producing a SNCR/SCR solution.

First claim

1 . A method for producing a selective non-catalytic reduction/selective catalytic reduction (SNCR/SCR) solution, comprising the steps of:
a) reacting ammonia and carbon dioxide in a reactor, thereby obtaining an aqueous composition comprising urea and ammonium salts; b) processing the aqueous composition obtained in step a), thereby obtaining a first aqueous solution comprising urea, and a second aqueous solution comprising ammonium salts; and c) diluting the second aqueous solution comprising ammonium salts obtained in step b) with a third aqueous solution, thereby producing the SNCR/SCR solution.

2 . The method according to claim 1 , wherein the aqueous composition obtained in step c) comprises from 10 to 40 weight % of nitrogen, expressed as ammonia.

3 . The method according to claim 1 , wherein the aqueous composition obtained in step c) comprises from 5.0 to 35 weight % of carbon, expressed as carbon dioxide.

4 . The method according to claim 1 , wherein the aqueous composition obtained in step c) does not form crystals above 15° C.

5 . The method according to claim 1 , wherein the aqueous composition obtained in step c) has a boiling point of at least 35° C.

6 . The method according to claim 1 , wherein step b) comprises generating the first aqueous solution comprising urea and a gaseous stream comprising water, ammonia, and carbon dioxide, from the aqueous composition comprising urea and ammonium salts obtained in step a), and condensing the gaseous stream comprising water, ammonia, and carbon dioxide into the second aqueous solution comprising ammonium salts.

7 . The method according to claim 6 , wherein generating the first aqueous solution comprising urea and a gaseous stream comprising water, ammonia, and carbon dioxide, from the aqueous composition comprising urea and ammonium salts obtained in step a), is achieved by heating up the aqueous composition comprising urea and ammonium salts.

8 . The method according to claim 1 , wherein the amount of nitrogen comprised in the SNCR/SCR solution represents from 0.5 to 10% of the amount of nitrogen, introduced as ammonia, in a urea-producing plant.

9 . The method according to claim 1 , wherein the aqueous composition obtained in step c) comprises from 0.01 to 5.0 weight % of urea.

10 . The method according to claim 1 , wherein the third aqueous solution used in step c) is selected from the group consisting of demineralized water, steam condensate, process condensate, and any mixture thereof.

11 . (canceled)

12 . A urea-producing plant comprising:
a high pressure section; a low pressure section; and a return line for transporting a first aqueous solution comprising ammonium salts from the low pressure section to the high pressure section; characterized in that the urea-producing plant further comprises: a means for drawing out an amount of the first aqueous solution from the return line; and a means for mixing the first aqueous solution with a second aqueous solution.

13 . A urea-producing plant comprising:
a high pressure section; a low pressure section; a finishing section; and a return line for transporting a first aqueous solution comprising ammonium salts from the finishing section to the low pressure section; characterized in that the urea-producing plant further comprises: a means for drawing out an amount of the first aqueous solution from the return line; and a means for mixing the first aqueous solution with a second aqueous solution.

14 . The urea-producing plant according to claim 12 , further comprising:
a medium pressure section; a return line for transporting a third aqueous solution comprising ammonium salts from the low pressure section to the medium pressure section; a means for drawing out an amount of the third aqueous solution from the return line; and a means for mixing the third aqueous solution with a fourth aqueous solution.

15 . A method for adapting an existing urea-producing plant, comprising the steps of:
installing a means for drawing out an amount of a first aqueous solution comprising ammonium salts; and installing a means for mixing the first aqueous solution with a second aqueous solution.

Assignees

• Yara Int Asa

Inventors

• Porro Lino Giovanni
• Van Belzen Ruud
• Malo Patrice
• Kohnke Sven
• Rungger Werner
• Weigl Klaus
• Duponchel Vincent

Classifications

• B01D2251/2062

  Ammonia · CPC title

• B01D53/56

  Nitrogen oxides (B01D53/60 takes precedence) · CPC title

• C01C1/02

  Preparation, {purification} or separation of ammonia · CPC title

• C01C1/26

  Carbonates or bicarbonates of ammonium · CPC title

• B01D2251/206

  Ammonium compounds · CPC title