Abstract
Ammonia is a promising carbon-free hydrogen carrier, but incomplete ammonia dehydrogenation (cracking) generates atmospheric emissions of NOx, a potent greenhouse gas. Additionally, incomplete cracking of ammonia leads to regulatory challenges in nuclear and fusion power, where tritiated ammonia (NT3) emissions are strictly controlled. Therefore, we report the use of low-temperature ammonia dehydrogenation catalysts (3%Ru/1%Y/12%K/Al2O3) in a palladium alloy H2 permeation membrane for quantitative conversion of ammonia into hydrogen and nitrogen at industry-relevant conditions. This catalytic membrane reactor system achieved an astonishing effluent concentration of <1 ppm at 450°C under a 100% NH3 stream, which is far beyond the 99.6% conversion target required for the adoption of ammonia as a vehicle fuel. The low-temperature ammonia dehydrogenation catalyst was tested in a packed bed reactor with NH3 and ND3 to both elucidate the reaction mechanism and to quantify the kinetic isotope effect of the membrane reactor. The rate-limiting step at temperatures relevant to the palladium membrane are isotope independent, indicating that the isotopologue content will not modify the desired reaction kinetics. By reducing emissions to below-trace levels with no additional separation, this work provides a path to greatly simplified and miniaturized ammonia cracking processes.
| Original language | English |
|---|---|
| Article number | e202500480 |
| Journal | ChemistryOpen |
| Volume | 15 |
| Issue number | 1 |
| DOIs | |
| State | Published - Jan 2026 |
Funding
This study was supported by National Nuclear Security Administration and U.S. Department of Energy (89303321CEM000080). This work was supported by the Tritium Modernization Program, sponsored by the National Nuclear Security Administration (NNSA) of the U.S. Department of Energy (DOE) through the Office of Strategic Materials Production Modernization. This work was produced by Battelle Savannah River Alliance, LLC, under Contract No. 89303321CEM000080 with the U.S. Department of Energy. Publisher acknowledges the U.S. Government license to provide public access under the DOE Public Access Plan (http://energy.gov/downloads/doe-public-access-plan). L.T.K. acknowledges support by the US Department of Energy, Office of Science, Basic Energy Sciences, Materials Sciences, and Engineering Division [FWP#ERKCK60]. This study was supported by National Nuclear Security Administration and U.S. Department of Energy (89303321CEM000080).
Keywords
- ammonia decomposition
- catalysis
- fusion
- hydrogen carrier
- membrane reactor
- ruthenium