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The amount of charge transfer generated by the degradation of FA could be obtained by reducing the Q th of added methanol from the Q net of mixture calculated from the I t curves according to the Eq. 2.
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Experimental methane yields were always higher than the BMP values of mixtures calculated from the BMP of each substrate, highlighting the importance of endogenous production (methane produced from auto-degradation of microbial community and generated solids).
Diffusion coefficients of n-C4H10 and CH4 in mixtures were calculated from mixture permeability and mixture solubility data.
Dye concentration in the reaction mixture was calculated from the calibration curve.
Heat capacity of the eutectic salt mixture was calculated from DSC curves as function of temperature in the reference of sapphire standard material.
The individual affinity of each lipid for SUMO-2 in the mixture was calculated from a global analysis of the combined data (Fig. 3b).
The relative ratio of hydrolysis products in the reaction mixtures were calculated from the peak area percentages in HPLC analysis without consideration of the detector response factor.
The Pi content of the pyruvate carboxylation reaction mixtures was calculated from the standard curve.
Adsorption excess isotherms of binary liquid mixtures have been calculated from synthetic adsorption energy distribution functions characterizing energetic heterogeneity at the liquid/solid interface.
The standard Gibbs energies of transfer of 1 mol of Zn2+ ions from water to PD-water mixtures (ΔG0t) were calculated from the reversible half-wave potentials referred to the Fic+/Foc scale and their values were always negative, indicating a higher stability of Zn2+ in aqueous PD solutions than in pure water due to the preferential solvation of Zn2+ by PD.
In case of complex product mixtures, conversions were calculated from respective relative peak areas of substrates.
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