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The final catalyst is motivation.
The final catalyst is thoroughly characterized and its catalytic and mechanical behavior is evaluated.
The amount of Pt loading was 0.3 wt%, so the final catalyst is denoted as 0.3Pt/USY.
The final catalyst is sensitive to whether reduction has taken place in hydrogen or butane, with the more effective dehydrogenation catalyst being generated from a hydrogen reduction.
Since Co acts as a promotor, a close interaction between Co and Mo in the final catalyst is of major importance for the catalytic activity.
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The effect of the silicon ortho- to pyrophosphate ratio on the final catalyst was investigated by variation of key catalyst preparation parameters, namely: H3PO4 concentration, impregnation and calcination temperature and water addition.
Moreover, (iv) the effects of heat treatment of the catalysts in H2 at 185 °C and in air at 185 275 °C on the surface chemistry of the support, surface morphology of the metallic component, and the performances of the final catalyst were investigated.
The final catalysts were tested in the CO oxidation reaction in presence of H2.
The final catalysts are obtained by annealing the impregnated samples in a H2 enriched atmosphere.
The physicochemical properties of the final catalysts were determined by using different techniques: N2 adsorption desorption isotherms, X-ray diffraction (XRD), inductively coupled plasma atomic emission spectroscopy (ICP-AES) and transmission electron microscopy (TEM).
A dimensional analysis of the model equations showed that the final catalyst profile is determined by three dimensionless groups, which describe the relative strength of convection, diffusion, and adsorption.
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