The controllable incorporation of multiple immiscible elements into a single nanoparticle merits untold scientific and technological potential, yet remains a challenge using conventional synthetic techniques. We present a general route for alloying up to eight dissimilar elements into single-phase solid-solution nanoparticles, referred to as high-entropy-alloy nanoparticles (HEA-NPs), by thermally shocking precursor metal salt mixtures loaded onto carbon supports [temperature ~2000 kelvin (K), 55-millisecond duration, rate of ~10 K per second]. We synthesized a wide range of multicomponent nanoparticles with a desired chemistry (composition), size, and phase (solid solution, phase-separated) by controlling the carbothermal shock (CTS) parameters (substrate, temperature, shock duration, and heating/cooling rate). To prove utility, we synthesized quinary HEA-NPs as ammonia oxidation catalysts with ~100% conversion and >99% nitrogen oxide selectivity over prolonged operations.
Nanoceria-supported
atomic Pt catalysts (denoted as Pt1@CeO2) have
been synthesized and demonstrated with advanced
catalytic performance for the nonoxidative, direct conversion of methane.
These catalysts were synthesized by calcination of Pt-impregnated
porous ceria nanoparticles at high temperature (ca. 1000 °C),
with the atomic dispersion of Pt characterized by combining aberration-corrected
high-angle annular dark-field scanning transmission electron microscopy
(HAADF-STEM), X-ray photoelectron spectroscopy (XPS), X-ray absorption
spectroscopy (XAS), and diffuse reflectance infrared Fourier transform
spectroscopy (DRIFTS) analyses. The Pt1@CeO2 catalysts exhibited much superior catalytic performance to its nanoparticulated
counterpart, achieving 14.4% of methane conversion at 975 °C
and 74.6% selectivity toward C2 products (ethane, ethylene,
and acetylene). Comparative studies of the Pt1@CeO2 catalysts with different loadings as well as the nanoparticulated
counterpart reveal the single-atom Pt to be the active sites for selective
conversion of methane into C2 hydrocarbons.
Selective conversion of methane (CH4) into value-added chemicals represents a grand challenge for the efficient utilization of rising hydrocarbon sources. We report here dimeric copper centers supported on graphitic carbon nitride (denoted as Cu2@C3N4) as advanced catalysts for CH4 partial oxidation. The copper-dimer catalysts demonstrate high selectivity for partial oxidation of methane under both thermo- and photocatalytic reaction conditions, with hydrogen peroxide (H2O2) and oxygen (O2) being used as the oxidizer, respectively. In particular, the photocatalytic oxidation of CH4 with O2 achieves >10% conversion, and >98% selectivity toward methyl oxygenates and a mass-specific activity of 1399.3 mmol g Cu−1h−1. Mechanistic studies reveal that the high reactivity of Cu2@C3N4 can be ascribed to symphonic mechanisms among the bridging oxygen, the two copper sites and the semiconducting C3N4 substrate, which do not only facilitate the heterolytic scission of C-H bond, but also promotes H2O2 and O2 activation in thermo- and photocatalysis, respectively.
Ethylene oxidation by Ag catalysts
has been extensively investigated over the past few decades, but many
key fundamental issues about this important catalytic system are still
unresolved. This overview of the selective oxidation of ethylene to
ethylene oxide by Ag catalysts critically examines the experimental
and theoretical literature of this complex catalytic system: (i) the
surface chemistry of silver catalysts (single crystal, powder/foil,
and supported Ag/α-Al2O3), (ii) the role
of promoters, (iii) the reaction kinetics, (iv) the reaction mechanism,
(v) density functional theory (DFT), and (vi) microkinetic
modeling. Only in the past few years have the modern catalysis research
tools of in situ/operando spectroscopy and DFT calculations been applied
to begin establishing fundamental structure–activity/selectivity
relationships. This overview of the ethylene oxidation reaction by
Ag catalysts covers what is known and what issues still need to be
determined to advance the rational design of this important catalytic
system.
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