6 research outputs found
Time-Resolved XANES Studies on Used Silica Supported Cobalt Catalysts
In order to investigate the phases of used Co/SiO2 catalysts, one of the most commonly used catalysts for Fischer-Tropsch synthesis, time-resolved X-ray absorption near edge structure (TR-XANES) technique was introduced. The catalysts were prepared by incipient wetness impregnation method with %Co loading of 15% and 20% and used for Fischer-Tropsch synthesis at the reaction temperature of 190oC and the pressure of 10 and 20 bar, called 15%Co/Aerosil_wi_used_10_bar, 15%Co/Aerosil_wi_used_20_bar, and 20%Co/Aerosil_wi_used_20_bar. TR-XANES showed the edge energy of 7721 eV for all used catalysts and by looking at the feature of their spectra, the results implied that the major phase was CoO. To further investigate their ability of being oxidized at elevated temperatures, the catalysts were oxidized by heating from ambient to 450oC with the heating rate of 8oC/min at the pressure of 1 bar with the O2:N2 flow rate of 70:30 ml/min. Once reaching 450oC, the temperature was held at 450oC for 90 min before cooling down to room temperature. During heating, holding, and cooling, the catalyst properties were measured by TR-XANES. When all catalysts heating up from 300 to 400oC, the edge energy of 15%Co/Aerosil_wi_used_10_bar, 15%Co/Aerosil_wi_used_20_bar, and 20%Co/Aerosil_wi_used_20_bar at 7719, 7717, and 7718 eV, respectively, showed the mixed phases of Co3O4 and CoO. There were no significant changes in phase while holding the temperature at 450oC. Once cooling from 450oC to room temperature, the edge energy of 15%Co/Aerosil_wi_used_10_bar at 7724 eV showed the main Co3O4 phase, the ones of 15%Co/Aerosil_wi_used_20_bar and 20%Co/Aerosil_wi_used_20_bar at 7717 and 7718 eV showed the mixed phase of Co3O4 and CoO. All results would be confirmed by further studies on temperature programmed oxidation (TPO)
Three-Dimensional Hierarchical Porous TiO2 for Enhanced Adsorption and Photocatalytic Degradation of Remazol Dye
Three-dimensional hierarchical mesoporous structures of titanium dioxide (3D-HPT) were synthesized by self-assembly emulsion polymerization. Polymethyl methacrylate (PMMA) and pluronic 123 (P123) were used as the soft templates and co-templates for assisting the formation of hierarchical 3D porous structures. The TiO2 crystal structure, morphology, and Remazol red dye degradation were investigated. The 3D-HPT and normal three-dimensional titanium dioxide (3D-T) presented the good connection of the nanoparticle-linked honeycomb within the form of anatase. The 3D-HPT structure showed greatly enhanced adsorption of Remazol dye, and facilitated the efficient photocatalytic breakdown of the dye. Surprisingly, 3D-HPT can adsorb approximately 40% of 24 ppm Remazol dye in the dark, which is superior to 3D-T and the commercial anatase at the same condition (approx. 5%). Moreover, 3D-HPT can completely decolorize Remazol dye within just 20 min, which is more than three folds faster than the commercial anatase, making it one of the most active photocatalysts that have been reported for degradation of Remazol dye. The superior photocatalytic performance is attributed to the higher specific surface area, amplified light-harvesting efficiency, and enhanced adsorption capacity into the hierarchical 3D inverse opal structure compared to the commercial anatase TiO2
Rate Enhancements in Structural Transformations of Pt–Co and Pt–Ni Bimetallic Cathode Catalysts in Polymer Electrolyte Fuel Cells Studied by in Situ Time-Resolved X‑ray Absorption Fine Structure
In situ time-resolved X-ray absorption
fine structure spectra of Pt/C, Pt<sub>3</sub>Co/C, and Pt<sub>3</sub>Ni/C cathode electrocatalysts in membrane electrode assemblies (catalyst
loading: 0.5 mg<sub>metal</sub> cm<sup>–2</sup>) were successfully
measured every 100 ms for a voltage cycling process between 0.4 and
1.0 V. Systematic analysis of in situ time-resolved X-ray absorption
near-edge structure and extended X-ray absorption fine structure spectra
in the molecular scale revealed the structural kinetics of the Pt
and Pt<sub>3</sub>M (M = Co, Ni) bimetallic cathode catalysts under
polymer electrolyte fuel cell operating conditions, and the rate constants
of Pt charging, Pt–O bond formation/breaking, and Pt–Pt
bond breaking/re-formation relevant to the fuel cell performances
were successfully determined. The addition of the 3d transition metals
to Pt reduced the Pt oxidation state and significantly enhanced the
reaction rates of Pt discharging, Pt–O bond breaking, and Pt–Pt
bond re-forming in the reductive process from 1.0 to 0.4 V
Kinetics and Mechanism of Redox Processes of Pt/C and Pt<sub>3</sub>Co/C Cathode Electrocatalysts in a Polymer Electrolyte Fuel Cell during an Accelerated Durability Test
The degradation of Pt electrocatalysts
in membrane electrode assemblies
(MEAs) of polymer electrolyte fuel cells under working conditions
is a serious problem for their practical use. Here we report the kinetics
and mechanism of redox reactions at the surfaces of Pt/C and Pt<sub>3</sub>Co/C cathode electrocatalysts during catalyst degradation
processes by an accelerated durability test (ADT) studied by operando
time-resolved X-ray absorption fine structure (XAFS) spectroscopy.
Systematic analysis of a series of Pt L<sub>III</sub>-edge time-resolved
XAFS spectra measured every 100 ms at different degradation stages
revealed changes in the kinetics of Pt redox reactions on Pt/C and
Pt<sub>3</sub>Co/C cathode electrocatalysts. In the case of Pt/C,
as the number of ADT cycles increased, structural changes for Pt redox
reactions (charging, surface, and subsurface oxidation) became less
sensitive because of the agglomeration of catalyst particles. It was
found that their rate constants were almost constant independent of
the agglomeration of the Pt electrocatalyst. On the other hand, in
the case of Pt<sub>3</sub>Co/C, the rate constants of the redox reactions
of the cathode electrocatalyst gradually reduced as the number of
ADT cycles increased. The differences in the kinetics for the redox
processes would be differences in the degradation mechanism of these
cathode electrocatalysts