Method for the cleaning of exhaust gas from a compression ignition engine

Patent metadata

Field	Value
Publication number	US-10399036-B2
Application number	US-201515116347-A
Country	US
Kind code	B2
Filing date	Feb 20, 2015
Priority date	Feb 28, 2014
Publication date	Sep 3, 2019
Grant date	Sep 3, 2019

Abstract

A method for the cleaning of exhaust gas from a compression ignition engine, comprising the steps of injecting a first amount of an aqueous urea solution into the gas; in a first mode of operation and at an exhaust gas temperature of between 150 and 220° C. hydrolysing the first amount of urea to ammonia reducing agent in presence of a first catalyst comprising vanadium oxide supported on titania and subsequently removing part of nitrogen oxides contained in the exhaust gas by contacting the gas mixed with the ammonia reducing agent through a second catalyst comprising platinum on titania and/or alumina; and in a second mode of operation and at an exhaust gas temperature above 220° C. removing a part of the nitrogen oxides in presence of the first catalyst and the ammonia reducing agent and subsequently oxidising hydrocarbons, carbon monoxide and remaining amount of the ammonia reducing agent further contained in the exhaust gas by passing the gas through the second catalyst.

First claim

The invention claimed is:

1. A method for the cleaning of an exhaust gas from a compression ignition engine, comprising the steps of
injecting an aqueous urea solution into the exhaust gas upstream of a first catalyst, which is a selective catalytic reduction (SCR) catalyst comprising vanadium oxide supported on titania, said first catalyst is close coupled with a second catalyst, which is a diesel oxidation (DOC) catalyst comprising platinum on titania and/or alumina, and said first catalyst is arranged close to the compression ignition engine such that exhaust gas therefrom heats the first catalyst to a first temperature resulting in catalytic hydrolysis of aqueous urea into ammonia and then heats the first catalyst to a second temperature resulting in catalytic reduction of NOx, whereby
in a first mode of operation the exhaust gas comprising the aqueous urea solution reaches an exhaust gas temperature of between 150 and 220° C. and (a) the aqueous urea solution is catalytically hydrolysed to an ammonia reducing agent by contacting with the first catalyst and (b) a part of the nitrogen oxides contained in the exhaust gas are subsequently removed in the exhaust gas mixed with the ammonia reducing agent by contacting with the second catalyst arranged downstream of the first catalyst; and
in a second mode of operation the exhaust gas comprising the aqueous urea solution reaches an exhaust gas temperature above 220° C. and (a) the aqueous urea solution is decomposed to the ammonia reducing agent and a part of the nitrogen oxides contained in the exhaust gas is removed by reacting the part of the nitrogen oxides with the ammonia reducing agent in presence of the first catalyst and (b) subsequently oxidising hydrocarbons, carbon monoxide, and ammonia in the exhaust gas leaving the first catalyst by contacting the exhaust gas with the second catalyst.

2. The method of claim 1 , wherein the first catalyst further comprises tungsten oxide.

3. The method of claim 1 , wherein the second catalyst further comprises palladium.

4. The method of claim 1 , wherein an ammonia oxidation catalyst is layered on at least part of the second catalyst.

5. The method of claim 4 , wherein the ammonia oxidation catalyst comprises platinum and zeolites promoted with iron and/or copper.

6. The method of claim 1 , wherein the first catalyst further comprises a zeolite SCR catalyst.

7. The method of claim 6 , wherein the zeolite SCR catalyst comprises at least one of Y-zeolite, beta-zeolite, SAPO-zeolites and chabazites.

8. The method of claim 1 , wherein the first catalyst and second catalyst are arranged in a single catalyst unit.

Assignees

• Umicore Ag & Co Kg

Inventors

• GABRIELSSON Pär L T

Classifications

• F01N2900/1404

  Exhaust gas temperature · CPC title

• F01N3/208

  Control of selective catalytic reduction [SCR], e.g. by adjusting the dosing of reducing agent · CPC title

• F01N2610/02

  the substance being ammonia or urea · CPC title

• F01N3/101

  Three-way catalysts · CPC title

• F01N2370/04

  Zeolitic material · CPC title