An interest in the on-purpose production
of 1,3-butadiene (1,3-BD)
has grown, as a consequence of the decline in naphtha cracking for
the production of ethene and propene, products that can now be produced
economically by thermal dehydrogenation of ethane and propane contained
in natural gas. In this study, the mechanism and kinetics of n-butane dehydrogenation to 1,3-BD are explored over atomically
distributed Pt sites grafted onto dealuminated zeolite BEA (DeAlBEA)
in the form of (Si–O–Zn)4–6Pt complexes. Reaction of n-butane dehydrogenation
carried out at 823 K with 2.53 kPa n-butane/He and
a weight-hourly space velocity (WHSV) of 14.5 h–1 produced 1,3-BD with a turnover frequency of 0.45 mol 1,3-BD (mol
Pt)−1 s–1. Space-time studies
and identification of the reaction intermediates suggest that n-butane first undergoes dehydrogenation primarily to 1-butene,
which then rapidly isomerizes to produce an equilibrated mixture of
1-butene and 2-butene. 1-Butene then undergoes secondary dehydrogenation
to produce 1,3-BD. We report, here, a detailed study of the kinetics
of n-butane dehydrogenation to butenes and 1-butene
dehydrogenation to 1,3-BD over isolated Pt sites. Both reactions exhibit
a Langmuir–Hinshelwood dependence on n-butane
and 1-butene partial pressures, respectively. Comparison of effective
forward rate constants of n-butane dehydrogenation
to butenes (k
1f) and butene dehydrogenation
to 1,3-BD (k
2f) shows that the isolated
Pt sites grafted onto DeAlBEA exhibit a very high activity for sequential
dehydrogenation of n-butane to 1,3-BD relative to
other Pt-based catalysts previously reported.