Solid acid catalysts are critical for green chemical transformations such as alcohol upgrading to sustainable aviation fuel and biomass depolymerization. These catalyst surfaces contain Brønsted and/or Lewis acid sites, and the strength of each site dictates the reaction rates, e.g., for alcohol dehydration. Previous studies have established a framework to predict solid Brønsted acid strength,
[1] but for Lewis acids, their strength is only understood in the homogeneous phase; this latter framework is incomplete for a structurally-complex heterogeneous surface with unknown active site coordination environments. Here, we establish both the Born-Haber thermochemical framework and experimental technique for assessing the Lewis acid strength of a solid acid catalyst,
[2] where we construct a scaling relation between 2-butanol intramolecular dehydration activation enthalpies and pyridine adsorption enthalpies—derived from kinetic results—as a function of the electronic chemical potential of metal-oxygen site pairs. Spanning a wide range from acidic (Al
2O
3) to basic (ZnO) metal oxides, 2-butanol C-O bond activation enthalpies increase by over 180 kJ mol
-1, coupled with pyridine adsorption enthalpies that increase by over 100 kJ mol
-1. From this scaling relation, we can estimate the 2-butanol dehydration rates for a wide range of temperatures of any solid acid catalyst simply from pyridine temperature-programmed desorption experiments. Using this scaling relation, we can also distinguish between Brønsted and Lewis acid site identities, because C-O scission transition state structures differ between the two acid sites: for 2-butanol dehydration, C-O scission reactions proceed through loosely-bound [H
2O···C
4H
9+···A
-]
‡ states on Brønsted acids and tightly-bound [CH
3CH(H···O-M)(CH
3)CH
+···
-O(H)]
‡ states on Lewis acids. This difference manifests as distinct enthalpy-entropy compensation lines, with a lower isokinetic temperature for Brønsted acids versus Lewis acids.
[1] Macht, J.; Carr, R. T.; Iglesia, E. Journal of Catalysis 2009, 264, 54–66.
[2] Broomhead, W. T.; Chin, Y.-H. ACS Catalysis 2024, 14, 2235–2245.