We report on the effect of catalyst support particle
porosity on
the conversion of NH3 synthesis from N2 and
H2 in a coaxial dielectric barrier discharge (DBD) plasma
reactor. The discharge was created using an AC applied voltage with
the reactor at room temperature and near atmospheric pressure (550
Torr). Two different particles of almost equal diameter (∼1.5
mm)porous silica (SiO2) ceramic beads (average
pore size: 8 nm) and smooth, nonporous soda lime glass beadswere
compared in the DBD reactor. As the pore size in the SiO2 particles was smaller than the Debye length, penetration of the
plasma into the pores of the particles was unlikely; however, reactive
species generated in the plasma outside the particles could diffuse
into the pores. The N2 conversion and energy yield of NH3 increased with applied voltage for both particle types, and
these values were consistently higher when using the SiO2 beads. Discharge and plasma properties were estimated from Lissajous
plots and using calculations with the BOLSIG+ software. The effect
of these two different catalyst supports on the physical properties
of the discharge was negligible. High resolution optical emission
spectra revealed that the concentrations of N2
+, atomic N, and atomic H (Hα, Hβ) in the plasma discharge were lower with the porous SiO2 beads than with the glass beads at every applied voltage tested.
This indicates that these active species participate in heterogeneous
reactions at support particle surfaces and that the larger surface
area presented by the porous particles led to higher rates of depletion
of these intermediates and a higher rate of ammonia synthesis.