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At higher temperatures, reaction of the intercalated lithium takes place, controlled by Li+-ion diffusion.
The study took into account the effects of variables temperatures, reaction times and H2SO4 concentration on hydrolysis using an incomplete factorial design.
The objective of this study is to investigate the relationship between the reaction temperatures, reaction time and methanol to oil molar ratio in the pre-treatment step.
Reaction conditions at different temperatures: reaction feed = 20 wt% LA, feed flow = 0.5 mL/h, N2 flow = 30 mL/h, catalyst CeP(2.5) = 300 mg and WHSV = 1.74 h−1.74
The simulation model predicts the effect of changing reaction temperatures, reaction pressures, catalyst pellet size, and the feed CO composition on pore diffusion, film heat transfer, internal heat transfer, and pressure drop.
A series of experiments employing varying temperatures, reaction times and stoichiometries gave meaningful insights into the mechanism of the chalcogenation.
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This mechanism includes a low temperature reaction group and a high temperature reaction group, linked with a transition temperature correlation.
Several key reaction conditions were studied, such as reaction temperature, reaction times, reaction mode (conventional or microwave irradiation).
Table 1 Oxidizing agent used in the reactive mixtures with H2SO4 and experimental conditions Agent HNO3 KNO 3 H2O2 KMnO4 Temperature reaction (°C) 40 30 40 30 Agent K2Cr2O7 NaIO4 NaClO3 Temperature reaction (°C) 30 40 30 .
The studied process parameters were reaction temperature, reaction time, catalyst concentration and PA MGO ratio.
Concentration of reactants, reaction temperature, reaction time, and current density were chosen as significant parameters.
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