Process for reducing the nitrogen oxide off-gas concentration in a nitric acid plant during shut-down and/or start-up, and nitric acid plant suitable therefor

Patent metadata

Field	Value
Publication number	US-9302222-B2
Application number	US-201314403149-A
Country	US
Kind code	B2
Filing date	May 2, 2013
Priority date	May 22, 2012
Publication date	Apr 5, 2016
Grant date	Apr 5, 2016

Abstract

Disclosed is a method and system for reducing the nitrogen oxide off-gas concentration in a nitric acid plant operated under pressure and equipped with a residual gas purification first reactor configured to remove nitrogen oxides from the off-gas during steady-state operation of the plant, and a second reactor configured to remove nitrogen oxides from the off-gas during a start-up and/or shut down of the plant. The method includes, during start-up and/or shut-down of the nitric acid plant, passing pressurized nitrogen-oxide-containing off-gas from the nitric acid plant and a gaseous reducing agent for the nitrogen oxides into the second reactor charged with a catalyst, to reduce the NOx content in the off-gas by at least catalytic reduction. Using the process and system, a colorless start-up and shut-down of nitric acid plants is possible and the nitrogen oxide content in the off-gas during start-up and/or shutdown can be substantially lowered.

First claim

The invention claimed is:

1. A method for reducing a nitrogen oxide off-gas concentration during at least one of a start-up or shutdown of a nitric acid manufacturing plant that is operated under pressure and is equipped with a residual gas cleaning first reactor configured to remove nitrogen oxides from off-gas during steady state operation of the plant, the method comprising:
initiating at least one of the start-up or shutdown of the nitric acid manufacturing plant;
directing a pressurized off-gas stream, containing nitrogen oxides from the nitrogen oxide plant and gaseous reducing agent for the nitrogen oxides, into a catalyst-filled second reactor configured to reduce the amount of nitrogen oxides in the off-gas during the at least one of the start-up or shutdown of the nitric acid manufacturing plant; and
reducing the NO x content in the off-gas by catalytic reduction in the catalyst-filled second reactor.

2. The method of claim 1 , further comprising, reducing the N 2 O content in the off-gas by at least one of catalytic reduction or catalytic decomposition in the catalyst-filled second reactor.

3. The method of claim 1 , wherein ammonia is the gaseous reducing agent for the nitrogen oxides.

4. The method of claim 1 , further comprising:
by a measurement device disposed at least one of upstream or downstream of the second reactor, measuring the content of nitrogen oxides in the off-gas stream during the at least one of the start-up or shutdown of the nitric acid plant; and
regulating the amount of reducing agent added to the off-gas stream based upon one or more control parameters including at least the measured content of the nitrogen oxide present in the off-gas stream.

5. The method of claim 1 , wherein a temperature in the second reactor, during the at least one of the shutdown or start-up of the nitric acid manufacturing plant, is in a range of between about 100° C. to about 600° C.

6. The method of claim 1 , wherein said step of directing a pressurized off-gas stream comprises:
directing, during the at least one of the start-up or shutdown of the nitric acid plant, the pressurized off-gas stream from the nitric acid plant to bypass a residual gas turbine that is used during steady state operation of the nitric acid plant; and
channeling the pressurized off-gas stream through the catalyst-filled second reactor that is connected in parallel to the residual gas turbine.

7. The method of claim 6 , further comprising, after said reducing the NO x content in the off-gas, sending the pressurized NO x -reduced off-gas stream to a chimney.

8. The method of claim 1 , wherein, during the at least one of the start-up or shutdown of the nitric acid plant, a pressure in the catalyst-filled second reactor is between about 0.9 bar to 3.0 bar.

9. The method of claim 1 , wherein a space velocity in the catalyst-filled second reactor varies between 2,000 h −1 and 200,000 h −1 .

10. The method of claim 1 , further comprising heating the pressurized off-gas stream during the at least one of the start-up or shutdown of the nitric acid plant, prior to the off-gas stream entering the catalyst-filled second reactor.

11. A nitric acid manufacturing system, comprising:
an ammonia oxidation system configured to produce nitrogen oxides NO x ;
an absorption tower in gaseous communication with said ammonia oxidation system, configured to produce nitric acid by reacting NO x , produced in said ammonia oxidation system, with water, and further configured to generate nitrogen oxide laden off-gas to be channeled to an off-gas stream;
a residual gas cleaning first reactor in gaseous communication with the off-gas stream from said absorption tower, said first reactor being configured to remove nitrogen oxides from the off-gas stream generated during a steady state operation of the nitric acid plant;
a residual gas turbine in gaseous communication with the off-gas stream from said residual gas cleaning first reactor;
a second reactor in gaseous communication with the off-gas stream from said residual gas cleaning first reactor, said second reactor being configured to reduce a content of nitrogen oxides in off-gas that is present or generated during at least one of a start-up or shutdown of the nitric acid manufacturing system, prior to reaching the steady state operation thereof, said second reactor including at least one catalyst disposed therein and configured to reduce the content of NO x in the off-gas stream by a reaction with a reducing agent; and
at least one inlet in communication with the off-gas stream sent from the residual gas cleaning first reactor and disposed upstream of the second reactor in an off-gas flow direction, said inlet being configured to introduce a reducing agent for nitrogen oxides into the off-gas stream prior to entering the second reactor.

12. The nitric acid manufacturing system of claim 11 , wherein said second reactor further includes at least one catalyst disposed therein and configured to reduce a content of N 2 O in the off-gas stream by a reaction with at least one of a reducing agent or a catalyst for decomposition of N 2 O to nitrogen and oxygen.

13. The nitric acid manufacturing system of claim 11 , further comprising a measurement device in communication with the off-gas stream and configured to determine a content of nitrogen oxides in the off-gas stream at a location in the off-gas stream that is at least one of upstream or down stream of said second reactor.

14. The nitric acid manufacturing system of claim 11 , further comprising a heating device disposed in the off-gas stream and configured to increase the temperature of the off-gas stream prior to entry of the off-gas stream into said second reactor.

15. The nitric acid manufacturing system of claim 11 , wherein said residual gas turbine and said second reactor are connected in parallel relative to said off-gas stream, wherein a flow path of the off-gas stream, during each of (a) the steady state operation and (b) the at least one of the start-up or shutdown of the nitric acid manufacturing system, is controlled by a plurality of valves in the flow path of the off-gas stream that are disposed upstream of each of the residual gas turbine and the second reactor.

16. The nitric acid manufacturing system of claim 11 , further comprising a reducing agent control valve disposed in said at least one inlet, and configured to control an amount of reducing agent supplied to the off-gas stream.

17. The nitric acid manufacturing system of claim 11 , wherein a volume of said second reactor is between about 0.01 m 3 to 10 m 3 .

Assignees

• Thyssenkrupp Ind Solutions Ag

Inventors

• Perbandt Christian

Classifications

• B01D2255/1025

  Rhodium · CPC title

• B01D2255/207

  Transition metals · CPC title

• B01D2251/208

  Hydrocarbons · CPC title

• B01D2255/1021

  Platinum · CPC title

• C01B21/40

  Preparation by absorption of oxides of nitrogen {(C01B21/26 takes precedence)} · CPC title