Sentence examples for molar number from inspiring English sources
In addition, based on these analyses, relationship between DMA, WAXS, TGA and conductivity parameters and either IEC or the molar number of tetrafluoroethylene (TFE) per comonomer unit are underlined, leading to a more comprehensive approach of architecture in perfluorosulfonic acid (PFSA) polymer membranes.
In this work, adsorption is modeled by the Langmuir adsorption equation given by n_{{{text{a}},{text{abs}}}} = n_{text{L}} frac{p}{{p + p_{text{L}} }} (3)where (n_{{{text{a}},{text{abs}}}}) is the molar number of absolute adsorbed gas; (n_{text{L}}) and (p_{text{L}}) are the Langmuir molar number and the Langmuir pressure, respectively.
Similar to Eq. (4), we have revised equation Eq. (5b) for Eq. (5a) n_{{{text{d}}, {text{ex}}}} = left( {1 - frac{{rho_{text{f}} }}{{rho_{text{d}}^{0} }}} right Kp times {text{TOC}} (5b where (rho_{text{d}}^{0}) is the dissolved gas density in kerogen; (n_{{{text{d}}, {text{ex}}}}) is the molar number of excessive dissolved gas.
Therefore, we use Henry's law to describe the dissolved gas n_{{{text{d}},{text{abs}}}} = Kp times {text{TOC}} (5a where (K) is the coefficient of Henry's law; (n_{{{text{d}},{text{abs}}}}) is the molar number of absolute dissolved gas.
So we have revised Eq. (4) n_{{{text{a}},{text{ex}}}} = left( {1 - frac{{rho_{text{f}} }}{{rho_{text{a}}^{0} }}} right)n_{text{L}} frac{p}{{p + p_{text{L}} }} (4 where (n_{{{text{a}},{text{ex}}}}) is the molar number of excessive adsorbed gas; (rho_{text{f}}) is the density of free gas; (rho_{text{a}}^{0}) is the maximum density of adsorbed gas at high pressures.
These test amplifications were performed from a set of cloned templates representing the entire target collection diluted to equivalent molar (target number) ratios.
Secondary outcomes were the first incidence of caries in mandibular or maxillary anterior teeth or molars and numbers of decayed, missing, or filled teeth at 18 months and 3 years, using the DMF (decayed, missing, filled) index.
The effect of feeding mode, reflux ratio, material molar ratio and number of reactive sections on the conversion of methyl acetate was investigated.
Micelle molar mass, association number and viscometric hydrodynamic radius increase with the length of the copolymer chain for a constant copolymer composition; however, the radius of gyration decreases.
Optimal conditions (at pH 5) gave chains with average number molar masses around 16,000 g mol−1 and polydispersity index close to 1.6, for a total conversion in polymer of about 60% after 2 h reaction.
A three dimensional graphical correlations of exergy lost to the ratio of liquid and gases molar flow (Lm/Gm), number of stages (N) and stage efficiency inside the column is presented at different operating states of an absorption column.
