Sentence examples for mol t from inspiring English sources

Open image in new window Fig. 4 Langmuir isotherm adsorption of C38 steel in 1 M HCl at different concentrations of inhibitor obtained by gravimetric analysis K_{text{ads}} = frac{1}{{C;({text{sol}})}}exp left( { - frac{{Delta G_{text{ads}} }}{RT}} right), (10 where R is the universal gas constant (8.314 J/K mol), T is the absolute temperature and C (sol) is the concentration of water (1000 g/L).

Where ?G? is the free energy change of the complex (kJ mol?1), R the gas constant (1.987 cal?mol?1 deg 1), T the temperature in Kelvin (273?+ C) and K c is the association constant of drug-acceptor complexes (1 mol?1 mol

In this equation, R represents the gas constant (8.314 J−1 mol K−1), T the absolute temperature, β the mean free energy, and ε the dye molecules moved to the solid surface.

Results show that the unreacted core kinetic model with formation of ashes describes the dissolution process of KFe3[ SO4 2 − X(CrO4 X](OH 6 in OH− medium Fig. 5 SEM image of partially decomposed particles in H3O+ medium (0.01 mol L−1, T = 50 °C, pH 2.01, d0 = 38 44 µm, CrO 4 −2  = 0.77 mol); a tr = 500 min; b tr = 1000 min; c tr = 1500 min; d tr = 2000 min.

A 162-mL titanium (IV) isopropoxide (0.5 M, Sigma-Aldrich) was rapidly injected into 290 mL of distilled water (15.5 mol, J. T Baker, Avantor Performance Materials, Center Valley, PA, USA) under stirring, and the solution was vigorously stirred for a further 10 h.

This approximate analytic solution agrees well with the result from the stochastic simulation over experimentally realistic range of N mol and t F when the rates are fixed to the rates of Dendra2 obtained from in vitro single-molecule experiments.

The S-tBA copolymers containing less than ca. 23 mol% t-butyl acrylate were found to be miscible with poly(2,6-dimethyl-1,4-phenylene 2,6-dimethyl-1,4-phenylene 2,6-dimethyl-1,4-phenylene 2,6-dimethyl-1,4-phenylenemetry studies.

CO conversion was increased from 9.1 mol% at T = 200 °C and H2/CO = 1 to 79.6 mol% at T = 240 °C and H2/CO = 2 and the yield and selectivity of DME also increased from 7.11% to 47.05% and 41.57% to 59.96%, (molar basis) respectively.

The default parameters simulate an experiment along the Z axis with a concentration in the input reservoir at initial time of 1711 mol m−3 (Cin (t) = 1711 mol m−3) and the concentration in the output reservoir at initial time being null (Cout (t) = 0).

The anodic rhodium dissolution was carried out in the individual urea melt and in the eutectic melt urea-NH4Cl (16.8 mol. %) (T = 130 °C).

where C t) is the MB concentration at the time t (mol m-3), t is the time (s) and k is the exponential decay constant (s-1).