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Furthermore, continuous EG steam reforming identified 3%Pt12%Ni/γ-alumina as the most stable catalyst.
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Structural models generated from NMR data showed that the most stable catalysts contained a significant fraction of furan rings and hardly any polycondensed aromatic rings.
PrFe0.7Ni0.3O3−δ was found to be the most active and stable catalyst due to the optimal composition of segregated Ni Fe alloy particles and redox properties of oxide matrix.
This system constitutes one of the most general, heterogeneous, highly stable catalyst, which does not require additives for activation and employs mild reaction conditions.
The 1%Rh/Ce-SBA-15 (Ce/Si = 1/20) is found to be the most active, selective and stable catalyst for CO2 reforming of ethanol to syngas or hydrogen.
The voltage during the galvanostatic electrolysis is well maintained for almost 400 h without any visible elevation, representing the few most stable noble-metal-free catalysts for water splitting.
The results of these experiments reveal that some of the mechanistic assumptions about the OCM reaction are not compatible with the nature of MnxOy-Na2WO4/SiO2, one of the most stable and best performing catalysts known for this reaction.
However, the 2% Cr catalyst which had the lowest initial conversion seems to be the most stable of the Cr modified catalysts.
Catalytic tests indicated higher hydrothermal stability of the FSP samples, whereas the corresponding Mn catalyst was most stable and most active.
The CuO-CeO2 catalyst batch which was calcined at 700 °C had the best activity because this catalyst formed the most stable state of Cu Ce–O solid solution and could chemisorb CO reversibly.
Additional stability evaluations performed over the Rh, Ni, and Co catalysts at 500 °C and 1 atm, under similar initial conversions, reveal the Co catalyst to be the most stable and selective towards H2 production.
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