We
investigated the influence of P incorporation into a Ni catalyst
on ethane dehydrogenation (EDH). Density functional theory calculations
on model Ni(111) and Ni2P(001) surfaces reveal that surface
P generally decreases adsorption energies of fragments relevant to
EDH at surface Ni sites but that P itself participates in binding
some of these intermediates. These nonlinear influences of P cause
CH3CH2–H activation to occur with similar
facility on metal and phosphide surfaces, while CH2CH–H
activation, an indicator of coking tendency, has much greater barriers
on the phosphide. We prepared Ni and Ni–P catalysts on an SBA-15
support to test these predictions. A Ni–P catalyst with a 2:1
ratio (Ni2P(2)/SBA-15), corresponding to the Ni2P phase, showed >80% ethylene selectivity during EDH at 873 K,
compared
to <1% ethylene selectivity on Ni/SBA-15, and maintained this selectivity
up to 4 h time-on-stream. Diffuse reflectance infrared Fourier transform
spectroscopy observations following ethylene exposure and heating
under an inert flow indicate the appearance of carbon deposits on
Ni/SBA-15 compared to ethylene desorption from Ni2P(2)/SBA-15,
consistent with predicted adsorption energy trends. Thermogravimetric
analysis of spent EDH catalysts indicates significantly less carbon
deposition on Ni2P(2)/SBA-15 relative to Ni/SBA-15. The
results highlight the potential of metal phosphides as selective and
robust alkane dehydrogenation catalysts.