Exhaust gas treatment system

Patent metadata

Field	Value
Publication number	US-12011690-B2
Application number	US-202117444633-A
Country	US
Kind code	B2
Filing date	Aug 6, 2021
Priority date	Aug 10, 2020
Publication date	Jun 18, 2024
Grant date	Jun 18, 2024

Abstract

An exhaust system for the treatment of an exhaust gas comprising a species to be treated, the system comprising: a first gas inlet for providing a flow of exhaust gas; a second gas inlet for providing a flow of heated gas; a plurality of sorbent beds for releasably storing the species; one or more catalysts for decomposing the species; first and second exhaust gas outlets; and a valve system configured to establish independently for each sorbent bed fluid communication in a first or second configuration, wherein: i) in the first configuration the flow of the exhaust gas from the first gas inlet contacts a sorbent bed for storing the species and then passes to the first gas outlet; and ii) in the second configuration the flow of heated gas from the second gas inlet contacts a sorbent bed for releasing the species, passes to one of the one or more catalysts and then passes to the second exhaust gas outlet; wherein the valve system is configured to ensure that at least one sorbent bed is in the first configuration and, preferably at least one other sorbent bed is in the second configuration.

First claim

The invention claimed is:

1. An exhaust system for the treatment of an exhaust gas comprising ammonia, the system comprising:
a first gas inlet for providing a flow of exhaust gas;
a second gas inlet for providing a flow of heated gas;
a plurality of sorbent beds, wherein each sorbent bed comprises an ammonia storage material for releasably storing ammonia, wherein the ammonia storage material is small-pore zeolite having a framework structure selected from the group consisting of AEI, AFT, AFV, AFX, AVL, CHA, EMT, GME, KFI, LEV, LTN, and SFW, including mixtures of two or more thereof;
one or more ammonia oxidation catalysts;
first and second exhaust gas outlets; and
a valve system configured to establish independently for each sorbent bed fluid communication in a first or second configuration, wherein:
i) in the first configuration the flow of the exhaust gas from the first gas inlet contacts a sorbent bed for storing ammonia and then passes to the first gas outlet; and
ii) in the second configuration the flow of heated gas from the second gas inlet contacts a sorbent bed for releasing the species, passes to one of the one or more ammonia oxidation catalysts and then passes to the second exhaust gas outlet;

wherein the valve system is configured to ensure that at least one sorbent bed is in the first configuration and, at least one other sorbent bed is in the second configuration.

2. The exhaust system according to claim 1 , wherein exhaust gas comprises from 1 to 5000 ppm of ammonia.

3. The exhaust system according to claim 1 , wherein the second gas inlet incorporates a heating device for providing the flow of heated gas.

4. The exhaust system according to claim 3 , wherein the heating device is configured to provide a flow of gas at a temperature of from 100 to 600° C.

5. The exhaust system according to claim 1 , wherein an exhaust gas is supplied to both the first and second gas inlets, or wherein the second gas inlet is an air inlet.

6. The exhaust system according to claim 1 , wherein the system further comprises one or more material filters to pre-filter the exhaust gas.

7. The exhaust system according to claim 1 , wherein the system comprises a contaminant sorbent material upstream of the plurality of sorbent beds, wherein the contaminant is selected from one or more of As, SO 2 , SO 3 , H 2 S, Hg and Cl.

8. The exhaust system according to claim 1 , wherein the valve system is configured to ensure that one sorbent bed is in the second configuration, and the remainder of the plurality of sorbent beds are in the first configuration.

9. The exhaust system according to claim 1 , the system further comprising one or more ammonia sensors in communication with each sorbent bed to determine an ammonia loading status.

10. The exhaust system according to claim 1 , comprising a heater wherein the heater is a propane, natural gas or biogas burner.

11. The exhaust system according to claim 10 , wherein a further heater is provided immediately upstream of the one or each ammonia oxidation catalyst.

12. The exhaust system according to claim 1 , wherein the valve system is further configured to establish independently for each sorbent bed fluid communication a third configuration for cooling of the sorbent bed, wherein gases are prevented from leaving the sorbent bed.

13. A livestock house, HVAC installation, waste water treatment plant, or a mine, comprising the exhaust-gas system according to claim 1 .

Assignees

• Johnson Matthey Plc
• Johnson Matthey Catalysts Germany Gmbh

Inventors

• Fedeyko Joseph
• Ferraro Anthony
• Koehler Kenneth
• Reichert Dirk
• Scherbel Harald
• Schreiber Harald
• Scullard Andrew
• Yeh Thomas

Classifications

• B01J2220/56

  Use in the form of a bed · CPC title

• B01J20/28014

  characterised by their form · CPC title

• B01D2257/708

  Volatile organic compounds V.O.C.'s · CPC title

• B01D2257/7025

  Methane · CPC title

• B01D2257/406

  Ammonia · CPC title