HT-H2-DeNOx II project (IGF):
Catalyzed NOx removal using H2 from the exhaust gas of GHG-neutral, lean H2 combustion engines for stationary and mobile applications
(ongoing)
The project presented here is the IGF follow-up project to “Catalytic NOx removal by H2 from the exhaust gas of GHG-neutral, lean H2-DI combustion engines for stationary and mobile applications” (duration: 10/2022-12/2024, FKZ: 01IF22407N).
The aim of the project is/was to develop an H2-deNOx catalyst for the exhaust gas of lean H2-DI combustion engines, which include trucks, heavy cars, ships and stationary applications, in particular CHP units. The engines mentioned are not yet available on the market, but require efficient exhaust gas aftertreatment for NOx for future legal certification.
The novelty of this catalytic deNOx approach was to use H2 as reducing agent in the entire range of typical exhaust gas temperatures (250 - 450 °C). The hydrogen required for NOx reduction is conceptually provided from the existing fuel tank.
In the previous project catalyst formulations were found that were tested under realistic conditions in the laboratory and exhibit H2-deNOx activity in the “high temperature range”, whereby the catalyst tests were primarily carried out at a relatively high H2 gas phase content of 1 vol.%. It is noteworthy, that the found catalysts do not only reduce NOx to N2, but also significantly to NH3. By this fact the possibility opened to use the NH3 formed for the reduction of still unconverted NOx on a downstream SCR catalyst. In a powder scale experiment this possibility could be confirmed successfully. The NH3 was used completely on a downstream Cu-Chabasite zeolite catalyst for the SCR reaction, which significantly increased the total NOx conversion. This was the first time, that a significant NOx reduction has been achieved without dosing NH3 or a NH3 precursor in a lean exhaust gas between 250 and 450 °C. It also could be shown, that the NOx conversion is strongly dependent on the H2 amount in the feed, i. e. in the presence of 0.2 and 0.5 % H2, the NOx conversion is correspondingly lower compared to 1% H2. However, similar to the low-temperature H2-deNOx reaction, N2O is also formed in the high-temperature range.
The catalysts used to achieve these results will now be used as a starting point for in-depth investigations and optimizations with regard to their composition in order to specifically increase deNOx activity and improve N2 and H2 selectivities, as well as for transfer to technically relevant honeycomb catalyst systems and pre-competitive evaluation. If this catalyst development is successful, H2-deNOx technology will be applicable not only in low-temperature but also in high-temperature ranges, meaning that lean H2 engines will no longer require the entire AdBlue SCR infrastructure.