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The maximum yield of oil + gas and the conversion level corresponding to the maximum yield can also be predicted easily.
As a result, the conversion level of steam reforming reaction is increased while byproduct formation of methane is suppressed.
The yield of light products (with boiling points less than 220 °C, or 430 °F) is usually reported as the conversion level for the unit.
While the presence of methane in the feed stream reduces the conversion level of CF3CH2F, it also modifies the polymer architecture.
The results are also compared with simpler model where reactor was considered as a black-box with the conversion level taken as constant data for each polymer grade.
The space velocity ranges from 427 to 460 h−1 to allow the conversion level small between 3 and 17 mol%.
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Although the conversion levels of both CBrF3 and CH4 can be predicted reasonably well, there are significant discrepancies over the product profiles of the reactions.
We attribute the contrast in the conversion levels of 44 and 27%% from the crystal structure determinations of the Pd and Pt systems, respectively, to the apparent lack of conversion of these species from the Raman data, which may be attributed to the time taken to run the experiments.
Interestingly, the decrease in particle size caused by 48 hours of agitation without added enzymes had little effect on the conversion levels achieved in the subsequent 48 hours of hydrolysis and the rate of conversion was mostly determined by the agitation rate during the hydrolysis.
Temperature dependent catalytic activity results revealed that at lower temperatures (<775 °C) the Cr-doped sample showed much higher activity while at higher temperatures (∼825 °C) the conversions levels were found to be similar on both the samples.
This process may continue well beyond the gelation of the α-phase, due to the low conversion level of the β-phase at the time the α-phase gels.
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