Ammonia storage set-point control for selective catalytic reduction applications
A system includes an injector control module and an SCR optimization module. The injector control module controls an amount of ammonia (NH 3 ) stored in a selective catalytic reduction (SCR) catalyst to maintain a first storage level. The SCR optimization module determines whether the first storage level maximizes a conversion efficiency of the SCR catalyst at a first temperature and minimizes a probability of NH 3 slip when the temperature of the SCR catalyst transitions from the first temperature to a second temperature. The injector control module controls the amount of NH 3 stored in the SCR catalyst to maintain a second storage level when the second storage level maximizes the efficiency of the SCR catalyst relative to the first storage level and minimizes the probability of NH 3 slip relative to the first storage level.
1. A system comprising:
an injector control module that controls an amount of ammonia (NH 3 ) stored in a selective catalytic reduction (SCR) catalyst to maintain a first storage level; and
an SCR optimization module that predicts whether a second storage level maximizes a conversion efficiency of the SCR catalyst and minimizes a probability of NH 3 slip when the temperature of the SCR catalyst transitions from a current temperature to a potential temperature,
wherein the injector control module increases an amount of reducing agent injected into exhaust gas to adjust the amount of NH 3 stored in the SCR catalyst from the first storage level to the second storage level at a current time when the second storage level is predicted to maximize the efficiency of the SCR catalyst relative to the first storage level and minimize the probability of NH 3 slip relative to the first storage level at a future time when the SCR catalyst is at the potential temperature.
2. The system of claim 1 wherein the injector control module controls the amount of NH 3 stored in the SCR catalyst to maintain the first storage level when the first storage level maximizes the efficiency of the SCR catalyst relative to the second storage level and minimizes the probability of NH 3 slip relative to the second storage level.
3. The system of claim 1 wherein the first storage level corresponds to a greater amount of NH 3 stored in the SCR catalyst than the second storage level.
4. The system of claim 1 wherein the second storage level corresponds to a greater amount of NH 3 stored in the SCR catalyst than the first storage level.
5. The system of claim 4 wherein the injector control module controls the amount of NH 3 stored in the SCR catalyst to maintain a third storage level when the third storage level maximizes the efficiency of the SCR catalyst relative to the first and second storage levels and minimizes the probability of NH 3 slip relative to the first and second storage levels.
6. The system of claim 5 wherein the third storage level corresponds to a lesser amount of NH 3 stored in the SCR catalyst than the first and second storage levels.
7. The system of claim 1 wherein the SCR optimization module determines the efficiency of the SCR catalyst and the probability of NH 3 slip based on an SCR model.
8. The system of claim 7 wherein, when the injector control module is controlling the amount of NH 3 stored in the SCR catalyst to maintain the first storage level, the SCR optimization module determines the efficiency of the SCR catalyst at the second storage level and the probability of NH 3 slip at the second storage level based on the SCR model.
9. A method comprising:
controlling an amount of ammonia (NH 3 ) stored in a selective catalytic reduction (SCR) catalyst to maintain a first storage level;
predicting whether a second storage level maximizes a conversion efficiency of the SCR catalyst and minimizes a probability of NH 3 slip when the temperature of the SCR catalyst transitions from a current temperature to a potential temperature; and
increasing an amount of reducing agent injected into exhaust gas to adjust the amount of NH 3 stored in the SCR catalyst from the first storage level to the second storage level at a current time when the second storage level is predicted to maximize the efficiency of the SCR catalyst relative to the first storage level and minimize the probability of NH 3 slip relative to the first storage level at a future time when the SCR catalyst is at the potential temperature.
10. The method of claim 9 further comprising controlling the amount of NH 3 stored in the SCR catalyst to maintain the first storage level when the first storage level maximizes the efficiency of the SCR catalyst relative to the second storage level and minimizes the probability of NH 3 slip relative to the second storage level.
11. The method of claim 9 wherein the first storage level corresponds to a greater amount of NH 3 stored in the SCR catalyst than the second storage level.
12. The method of claim 9 wherein the second storage level corresponds to a greater amount of NH 3 stored in the SCR catalyst than the first storage level.
13. The method of claim 12 further comprising controlling the amount of NH 3 stored in the SCR catalyst to maintain a third storage level when the third storage level maximizes the efficiency of the SCR catalyst relative to the first and second storage levels and minimizes the probability of NH 3 slip relative to the first and second storage levels.
14. The method of claim 13 wherein the third storage level corresponds to a lesser amount of NH 3 stored in the SCR catalyst than the first and second storage levels.
15. The method of claim 9 further comprising determining the efficiency of the SCR catalyst and the probability of NH 3 slip based on an SCR model.
16. The method of claim 15 further comprising determining the efficiency of the SCR catalyst at the second storage level and the probability of NH 3 slip at the second storage level based on the SCR model when controlling the amount of NH 3 stored in the SCR catalyst to maintain the first storage level.