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We investigated the effects of metallic surface area of Pt and imposed voltage.
Therefore, the cermet electrode has to possess a sufficient open porosity and the expanded metallic surface area exposed to pores as large as possible.
Results show that both the energy input and metallic surface area of Pt plays important roles for NO decomposition to N2 in the plasma catalyst system.
The two important characteristics of the metallic surface area of copper and the amount of acidic sites are well correlated with the intrinsic catalytic activity on this consecutive reaction.
The ruthenium metal areas were determined using the equation S CO = n m S X m n s −1, where S CO is the total metallic surface area, n m S is the CO consumption and X m is chemisorption stoichiometry at monolayer coverage, and n s −1 is the number of ruthenium atoms per unit surface area.
The palladium metal areas were determined using the equation SCO = nmS Xm ns−1, where SCO is the total metallic surface area, nmS is the CO consumption and Xm is chemisorption stoichiometry at monolayer coverage, and ns−1 is the number of palladium atoms per unit surface area.
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SRL and a lithographic polymer imprinting technique are used to produce nanowire or nanodot array model catalysts with metallic surface areas up to 1 cm2 or 1011 nanoparticles.
It was found that the metallic specific surface area increased linearly with increasing Ir concentration and that interstitial sites appeared for metal contents greater than 20%.
It is revealed that the active metallic Ni surface area, surface alkalinity and active oxygen abundance are the major factors deciding the reaction performance of the Ni/Mg-Al-O catalysts.
These results suggest that the hydrogen ingress caused instability of metallic surface, increasing the surface area activity.
Processes with metallic catalysts depend on the metal composition and the specific surface area of metallic materials.
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