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. 2023 Feb 20;11(9):3621-3632.
doi: 10.1021/acssuschemeng.2c05877. eCollection 2023 Mar 6.

Incorporation of a Metal Catalyst for the Ammonia Synthesis in a Ferroelectric Packed-Bed Plasma Reactor: Does It Really Matter?

Affiliations

Incorporation of a Metal Catalyst for the Ammonia Synthesis in a Ferroelectric Packed-Bed Plasma Reactor: Does It Really Matter?

Paula Navascués et al. ACS Sustain Chem Eng. .

Abstract

Plasma-catalysis has been proposed as a potential alternative for the synthesis of ammonia. Studies in this area focus on the reaction mechanisms and the apparent synergy existing between processes occurring in the plasma phase and on the surface of the catalytic material. In the present study, we approach this problem using a parallel-plate packed-bed reactor with the gap between the electrodes filled with pellets of lead zirconate titanate (PZT), with this ferroelectric material modified with a coating layer of alumina (i.e., Al2O3/PZT) and the same alumina layer incorporating ruthenium nanoparticles (i.e., Ru-Al2O3/PZT). At ambient temperature, the electrical behavior of the ferroelectric packed-bed reactor differed for these three types of barriers, with the plasma current reaching a maximum when using Ru-Al2O3/PZT pellets. A systematic analysis of the reaction yield and energy efficiency for the ammonia synthesis reaction, at ambient temperature and at 190 °C and various electrical operating conditions, has demonstrated that the yield and the energy efficiency for the ammonia synthesis do not significantly improve when including ruthenium particles, even at temperatures at which an incipient catalytic activity could be inferred. Besides disregarding a net plasma-catalysis effect, reaction results highlight the positive role of the ferroelectric PZT as moderator of the discharge, that of Ru particles as plasma hot points, and that of the Al2O3 coating as a plasma cooling dielectric layer.

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Conflict of interest statement

The authors declare no competing financial interest.

Figures

Figure 1
Figure 1
(a) Schematic of PZT, Al2O3/PZT, and Ru-Al2O3/PZT pellets. (b) Arrangements of the sets of pellets for the used barrier configurations. Ground and HV (high voltage) symbols refer to the electrical connections of bottom and top electrodes.
Figure 2
Figure 2
Analysis of the electric field distribution in the packed-bed barrier by means of Comsol Multiphysics simulations. (a) Distribution of the electric field between two equally separated pellets of PZT (top) and a PZT and a Al2O3/PZT pellet (bottom). The “r” line indicates the straight line selected to evaluate the electric field. (b) Electric field distribution along the line “r” for the PZT and Al2O3/PZT configurations.
Figure 3
Figure 3
(a) Sketch and (b) SEM micrographs of a Ru-Al2O3 coated PZT pellet. The dots in sketch (a) refer to Ru aggregates and the fact that it is distributed in the interior of the alumina coating layer. (c) SEM micrograph and (d) EDX analysis in the form of Al (red) and Ru (green) maps of the Al2O3-supported Ru catalyst powder.
Figure 4
Figure 4
Electrical characterization of the reactor for the three barrier configurations (PZT, Al2O3/PZT, and Ru-Al2O3/PZT). I(t) curves during plasma ignition at (a) ambient temperature (2.5 kV, 5 kHz) and (b) 190 °C (2.5 kV, 2 kHz). (c) - (d) Lissajous plots determined from the curves in (a) and (b), respectively.
Figure 5
Figure 5
Evolution at ambient temperature of (a) the reaction yield and (b) the energy efficiency for the NH3 synthesis reaction as a function of the applied voltage. Data corresponding to low reaction yields are plotted with empty dots and dash lines. Experiments were carried out at a frequency of 5 kHz. The star dot corresponds to a 7% nitrogen conversion in experiments reported in ref (31).
Figure 6
Figure 6
Evolution of (a) reaction yield and (b) energy efficiency for the ammonia synthesis reaction as a function of frequency. For the experiments at 1 kHz, results are plotted with empty dots and dash lines, indicating a possible inaccuracy in the determination of these values. Experiments were carried out at ambient temperature, a voltage amplitude of 2.5 kV, and a variable frequency between 1 and 5 kHz.
Figure 7
Figure 7
Evolution of (a) reaction yield and (b) energy efficiency for the ammonia synthesis reaction as a function of frequency. Experiments were carried out at 190 °C for a voltage amplitude of 2.5 kV and variable frequencies between 1 and 3 kHz. For comparison, data obtained under the same operating conditions at ambient temperature are included in the plot as dashed lines and faint colors.
Figure 8
Figure 8
OES spectra recorded at (a) ambient temperature (2.5 kV, 5 kHz) and (b) 190 °C (2.5 kV, 2 kHz).

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