| Home > Workflow collections > Publication Charges > Nucleation as a rate-determining step in catalytic gas generation reactions from liquid phase systems |
| Typ | Amount | VAT | Currency | Share | Status | Cost centre |
| APC | 4603.82 | 0.00 | EUR | 100.00 % | (Zahlung erfolgt) | ZB |
| Sum | 4603.82 | 0.00 | EUR | |||
| Total | 4603.82 |
| Journal Article | FZJ-2022-03731 |
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2022
Assoc.
Washington, DC [u.a.]
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Please use a persistent id in citations: http://hdl.handle.net/2128/33964 doi:10.1126/sciadv.ade3262
Abstract: The observable reaction rate of heterogeneously catalyzed reactions is known to be limited either by the intrinsic kinetics of the catalytic transformation or by the rate of pore and/or film diffusion. Here, we show that in gas generation reactions from liquid reactants, the nucleation of gas bubbles in the catalyst pore structure represents an additional important rate-limiting step. This is highlighted for the example of catalytic hydrogen release from the liquid organic hydrogen carrier compound perhydro-dibenzyltoluene. A nucleation-inhibited catalytic system produces only dissolved hydrogen with fast saturation of the fluid phase around the active site, while bubble formation enhances mass transfer by more than a factor of 50 in an oscillating reaction regime. Nucleation can be efficiently triggered not only by temperature changes and catalyst surface modification but also by a mechanical stimulus. Our work sheds new light on performance-limiting factors in reactions that are of highest relevance for the future green hydrogen economy.
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