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Figure 3 shows the Mg2+ substitution energy ΔE for a Ca2+ site as a function of depth for the interface of the {001} and {110} surfaces.
Combined activity and stability studies, ideally following the evolution of the active site as a function of catalyst treatment in real time are recommended.
Potential-invariant values of the constants for H2O2, H+ and O2 binding are determined and the rate constants for the reduction and the re-oxidation of the binding site as a function of potential are evaluated.
Moreover, the decomposition of the XPS spectral envelope is used to quantify the proportion of CoMoS phase and to normalize the catalytic activity in toluene-hydrogenation per edge site as a function of the Co/Mo ratio.
Open image in new window Fig. 4 a The ratio N w/N BH (the average number of water molecules per hydrated Brønsted acid site) as a function of time.
The boxplots in Fig. 2 show a summary of the variation of mean canopy height and FC derived from each data model at each study site as a function of plot size.
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There we plot the time-evolution of the number of doubly occupied sites as a function of time.
The MAE at three chosen lattice sites as a function of dose is shown in Fig. 12.
Figure 4 shows a typical solution for the fraction of exposed sites as a function of depth into the crystal at large times.
The convergence in the reconstruction of observations at different sites as a function of the number of components and its relation to the characteristics of the site are analysed.
The highest CO conversion was achieved using the 70Co30Fe/Al2O3 which also had the highest CO adsorption capacity. Figure 5 shows variation of CO conversion and number of active sites as a function of catalysts' compositions.
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