Ammonia is one of the most produced chemicals, mainly synthesized from fossil fuels for fertilizer applications. Furthermore, ammonia may be one of the energy carriers of the future, when it...
Plasma
catalysis is an emerging new technology for the electrification
and downscaling of NH3 synthesis. Increasing attention
is being paid to the optimization of plasma catalysis with respect
to the plasma conditions, the catalyst material, and their mutual
interaction. In this work we use microkinetic models to study how
the total conversion process is impacted by the combination of different
plasma conditions and transition metal catalysts. We study how plasma-generated
radicals and vibrationally excited N2 (present in a dielectric
barrier discharge plasma) interact with the catalyst and impact the
NH3 turnover frequencies (TOFs). Both filamentary and uniform
plasmas are studied, based on plasma chemistry models that provided
plasma phase speciation and vibrational distribution functions. The
Langmuir–Hinshelwood reaction rate coefficients (i.e., adsorption
reactions and subsequent reactions among adsorbates) are determined
using conventional scaling relations. An additional set of Eley–Rideal
reactions (i.e., direct reactions of plasma radicals with adsorbates)
was added and a sensitivity analysis on the assumed reaction rate
coefficients was performed. We first show the impact of different
vibrational distribution functions on the catalytic dissociation of
N2 and subsequent production of NH3, and we
gradually include more radical reactions, to illustrate the contribution
of these species and their corresponding reaction pathways. Analysis
over a large range of catalysts indicates that different transition
metals (metals such as Rh, Ni, Pt, and Pd) optimize the NH3TOFs depending on the population of the vibrational levels of N2. At higher concentrations of plasma-generated radicals, the
NH3 TOFs become less dependent on the catalyst material,
due to radical adsorptions on the more noble catalysts and Eley–Rideal
reactions on the less noble catalysts.
Plasma-catalytic ammonia synthesis is receiving ever increasing attention, especially in packed bed dielectric barrier discharge (DBD) reactors. The latter typically operate in the filamentary regime when used for gas conversion applications. While DBDs are in principle well understood and already applied in the industry, the incorporation of packing materials and catalytic surfaces considerably adds to the complexity of the plasma physics and chemistry governing the ammonia formation. We employ a plasma kinetics model to gain insights into the ammonia formation mechanisms, paying special attention to the role of filamentary microdischarges and their afterglows. During the microdischarges, the synthesized ammonia is actually decomposed, but the radicals created upon electron impact dissociation of N 2 and H 2 and the subsequent catalytic reactions cause a net ammonia gain in the afterglows of the microdischarges. Under our plasma conditions, electron impact dissociation of N 2 in the gas phase followed by the adsorption of N atoms is identified as a rate-limiting step, instead of dissociative adsorption of N 2 on the catalyst surface. Both elementary Eley−Rideal and Langmuir−Hinshelwood reaction steps can be found important in plasma-catalytic NH 3 synthesis.
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