Method for use in connection with an exhaust gas post-treatment system
A method for use with an exhaust gas post-treatment system on an internal combustion engine operated with air surplus includes reducing nitrous oxides in that an ammonia-separating reducing agent is added to the exhaust gas flow upstream of a catalyst which is charged with a catalyst material for selective catalytic reduction of nitrous oxides. The method further provides that the NH 3 to NO x ratio (feed ratio α) is varied in phases by changing the untreated nitrous oxide emissions of the internal combustion engine such that the feed ratio α oscillates in phases about a predefined value.
1. A method for an exhaust gas post-treatment system used with an internal combustion engine operated with air surplus, the method comprising:
reducing nitrous oxides by adding an ammonia-separating reducing agent to an exhaust gas flow upstream of an SCR catalyst which is charged with a catalyst material for selective catalytic reduction of nitrous oxides, and
varying a NH3 to NO x ratio (feed ratio α) in phases by periodically changing untreated NO x emissions of the internal combustion engine between phases of high untreated NO x emissions and low untreated NO x emissions such that the feed ratio oscillates in phases about a predefined value.
2. The method according to claim 1 , wherein a quantity of the reducing agent supplied during said step of adding is not adapted to the periodically changing untreated NO x emissions.
3. The method according to claim 1 , wherein said step of adding comprises reducing or interrupting completely the quantity of reducing agent in the phases with high untreated NO x emissions.
4. The method according to claim 1 , wherein said step of adding comprises raising a quantity of reducing agent in the phases with low untreated NO x emissions.
5. The method according to claim 1 , wherein the untreated NO x emissions are raised during said step of varying by changing one of a start of fuel injection, an air/fuel ratio, a fuel injection pressure, a number and temporal sequence of individual fuel injections during a working cycle, a quantity of recirculated exhaust gas, and an intake air temperature.
6. The method according to claim 1 , wherein said step of varying further comprises selecting at least one of a period length, an amount of rise, an amount of fall, a duration of rise, and a duration of fall of the untreated NO x emissions as a function of operating conditions of the exhaust gas post-treatment system.
7. The method according to claim 6 , wherein the operating conditions taken into account include at least one of a catalyst temperature, an ammonia charge level of the catalyst, an NO x conversion rate, untreated NO x emissions, an N0 2 quantity upstream of the SCR catalyst, NO x emissions downstream of the exhaust gas post treatment system, NH 3 emissions downstream of the exhaust gas post-treatment system, a supplied quantity of reducing agent, a stored NH 3 quantity, and an NH 3 quantity which can be stored.
8. The method according to claim 6 , wherein the operating conditions of the exhaust gas post-treatment system are determined by at least one of sensors and models in the form of mathematical functions, maps or neuronal networks.
9. The method according to claim 1 , further comprising the step of decomposing unconsumed NH 3 passing the SCR catalyst by a charge of material with oxidative action arranged on a clean gas side of the SCR catalyst.
10. The method according to claim 1 , wherein said step of varying comprises varying one of the untreated NO x emissions and the feed ratio α by at least 20%.
11. The method according to claim 10 , wherein said step of varying comprises varying one of the untreated NO x emissions and the feed ratio by at least 40%.
12. The method according to claim 11 , wherein said step of varying comprises varying one of the untreated NO x emissions and the feed ratio α by at least 60%.
13. An arrangement for performance of the method according to claim 1 , comprising an SCR catalyst in an exhaust flow, wherein a charge of the SCR catalyst with SCR active material is made such that an ammonia storage capacity of the SCR catalyst rises towards a clean gas side.