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Based on the mole fractions and formation temperatures of the detected pyrolysis species, a simple reaction network is deduced.
The measured solubility data at the temperature and pressure range of 308.15 338.15 K and 16 40 MPa was ranged between 2.65 × 10−5 and 8.12 × 10−4 based on the mole fraction.
Based on the mole fractions of H2SO4 for some of the extremely low pH solutions reported by Nordstrom et al.[25] and higher pH solutions more typically found in other AMD areas, the heat from mixing for several hypothetical scenarios can be calculated.
Regarding this fact, solubility of fluvoxamine maleate in supercritical carbon dioxide in wide ranges of temperature (308 338 K) and pressure (200 400 bar) was measured using a static method coupled with gravimetric method which is in the range of 1.23 × 10−5 to 4.45 × 10−4 based on the mole fraction.
The obtained solubility data were in the range of 1.17 × 10−5 and 5.12 × 10−4 based on the mole fraction (mole piroxicam/(mole piroxicam + mole CO2)) then modeled using four different density based correlations namely Bartle et al., Mendez-Santiago-Teja, Chrastil and Kumar and Johnston models.
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Solubility predictions (here expressed as a mole fraction) were based on the model developed by Freire et al. [25].
The values of turnover frequency (TOF) were calculated based on the FAL mole produced at per mol of active sites and per hour aZr-PhyA: Zr-phytic acid hybrid bZr-PN: organotriphosphate-zirconium hybrid cHydroxyapatite-encapsulated magnetic γ-Fe2O3.
Figure 9a shows the Nyquist plots of the cells based on the different mole ratios, in which the symbols are the experimental data and the solid lines are the fitting results.
The real fluid volume is equal to total volume of PVT cell (VT) determined in Appendix B. Ideal gas volume ( V ideal, j ) at pressure level j is calculated based on the remaining mole of reservoir fluid (nT,j) using Eq. 27.
When glucose or ethanol were used as carbon source, the biomass yield and PHB yield on the mixed-substrate in the feed medium was calculated based on the C-moles of consumed substrate.
Empirical relationships based on the NAPL-phase mole fraction and/or micelle-aqueous partition coefficients measured in single-component NAPL systems are developed to estimate values for the multicomponent partition coefficients.
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