11 research outputs found
Cation Segregation of A‑Site Deficiency Perovskite La<sub>0.85</sub>FeO<sub>3−δ</sub> Nanoparticles toward High-Performance Cathode Catalysts for Rechargeable Li‑O<sub>2</sub> Battery
Cation segregation
of perovskite oxide is crucial to develop high-performance catalysts.
Herein, we achieved the exsolution of α-Fe<sub>2</sub>O<sub>3</sub> from parent La<sub>0.85</sub>FeO<sub>3−δ</sub> by a simple heat treatment. Compared to α-Fe<sub>2</sub>O<sub>3</sub> and La<sub>0.85</sub>FeO<sub>3−δ</sub>, α-Fe<sub>2</sub>O<sub>3</sub>-LaFeO<sub>3–<i>x</i></sub> achieved
a significant improvement of lithium-oxygen battery performance in
terms of discharge specific capacity and cycling stability. The promotion
can be attributed to the interaction between α-Fe<sub>2</sub>O<sub>3</sub> and LaFeO<sub>3–<i>x</i></sub>. During
the cycling test, α-Fe<sub>2</sub>O<sub>3</sub>-LaFeO<sub>3–<i>x</i></sub> can be stably cycled for 108 cycles at a limited
discharge capacity of 500 mAh g<sup>–1</sup> at a current density
of 100 mA g<sup>–1</sup>, which is remarkably longer than those
of La<sub>0.85</sub>FeO<sub>3−δ</sub> (51 cycles), α-Fe<sub>2</sub>O<sub>3</sub> (21 cycles), and mechanical mixing of LaFeO<sub>3</sub> and α-Fe<sub>2</sub>O<sub>3</sub> (26 cycles). In general,
these results suggest a promising method to develop efficient lithium-oxygen
battery catalysts via segregation
Mechanistic Insight into Nanoarchitected Ag/Pr<sub>6</sub>O<sub>11</sub> Catalysts for Efficient CO Oxidation
Ag/Pr<sub>6</sub>O<sub>11</sub> catalysts supported by either Pr<sub>6</sub>O<sub>11</sub> nanorods (Pr<sub>6</sub>O<sub>11</sub>-NRs)
or nanoparticles (Pr<sub>6</sub>O<sub>11</sub>-NPs) were prepared
by conventional incipient wetness impregnation. The nanocomposite
of Ag/Pr<sub>6</sub>O<sub>11</sub>-NRs demonstrated a higher catalytic
activity for CO oxidation than Ag/Pr<sub>6</sub>O<sub>11</sub>-NPs
at lower temperatures. This improved performance may be ascribed to
the mesoporous features and resultant oxygen vacancies of the Pr<sub>6</sub>O<sub>11</sub> nanorods support, as well as the large surface
area and homogeneous loading of Ag species. As a result, 98.7 and
100% CO conversions were achieved at 210 and 240 °C for Ag/Pr<sub>6</sub>O<sub>11</sub>-NRs, while Ag/Pr<sub>6</sub>O<sub>11</sub>-NPs
require a temperature of 320 °C to obtain the 100% CO conversion
rate. These findings reveal that Pr<sub>6</sub>O<sub>11</sub>-NRs
is the preferable support, comparative to Pr<sub>6</sub>O<sub>11</sub>-NPs, for Ag/Pr<sub>6</sub>O<sub>11</sub> catalysts, for CO oxidation
Micro/nano hierarchical structured titanium treated by NH<sub>4</sub>OH/H<sub>2</sub>O<sub>2</sub> for enhancing cell response - Fig 2
<p>XPS survey date of SLA, E, SE surface(A) and XPS narrow spectra of O1s on SLA, E, SE surface(B).</p
Schematic of the interactions between bone and the implant surface at different topographical scales.
<p>Schematic of the interactions between bone and the implant surface at different topographical scales.</p
Micro/nano hierarchical structured titanium treated by NH<sub>4</sub>OH/H<sub>2</sub>O<sub>2</sub> for enhancing cell response - Fig 3
<p>Water contact angle on SLA, E, SE surface(A), CA<sub>0</sub>: fresh surface, CA<sub>t</sub>: exploded surface and Surface profiler test results of SLA, E, SE surface(B).</p
Micro/nano hierarchical structured titanium treated by NH<sub>4</sub>OH/H<sub>2</sub>O<sub>2</sub> for enhancing cell response - Fig 1
<p>Surface morphology of SLA(A), E(B), SE(C) samples.</p
The average area and number of MG63 cells attached to SLA, E, SE surface after cultured for 4 hours.
<p>A: Cytoskeleton rhodamine-phalloidin staining chart, the lower right corner for its enlarged image; B: The individual cell spreading area on the surface (*** P <0.001); C: Cell nucleus acridine orange(AO) staining; D: Cell counting(*P<0.05;***P<0.001).</p
Cell analysis on SLA, E, SE surface.
<p>A: Cell numbers after cultured for 24, 48 and 72 h; B: Cell viability after cultured for 24, 48 and 72 h; C: Relative activity of ALP after 7 d and 14 d of osteoinduction; D: OCN and RUNX2 production after 21-day osteoinduction(*P<0.05;**P<0.01;***P<0.001).</p
The corrosion mechanisms of H<sub>2</sub>SO<sub>4</sub> + HCl and NH<sub>4</sub>OH + H<sub>2</sub>O<sub>2</sub>.
<p>The corrosion mechanisms of H<sub>2</sub>SO<sub>4</sub> + HCl and NH<sub>4</sub>OH + H<sub>2</sub>O<sub>2</sub>.</p
Activation of Surface Oxygen Sites in a Cobalt-Based Perovskite Model Catalyst for CO Oxidation
Anionic
redox chemistry is becoming increasingly important in explaining
the intristic catalytic behavior in transition-metal oxides and improving
catalytic activity. However, it is a great challenge to activate lattice
oxygen in noble-metal-free perovskites for obtaining active peroxide
species. Here, we take La<sub>0.4</sub>Sr<sub>0.6</sub>CoO<sub>3‑δ</sub> as a model catalyst and develop an anionic redox activity regulation
method to activate lattice oxygen by tuning charge transfer between
Co<sup>4+</sup> and O<sup>2–</sup>. Advanced XAS and XPS demonstrate
that our method can effectively decrease electron density of surface
oxygen sites (O<sup>2–</sup>) to form more reactive oxygen
species (O<sup>2‑<i>x</i></sup>), which reduces the
activation energy barriers of molecular O<sub>2</sub> and leads to
a very high CO catalytic activity. The revealing of the activation
mechanism for surface oxygen sites in perovskites in this work opens
up a new avenue to design efficient solid catalysts. Furthermore,
we also establish a correlation between anionic redox chemistry and
CO catalytic activity