Sentence examples for solution is described by from inspiring English sources
end{aligned} We can see that the solution is described by the scalar (a(t),b(t)in mathbb{C}) and (r_{1}(t),r_{2}(t)inmathbf{C}(mathbb{R},mathbf{H}^{1})).
The latter case is covered by the above formulas (2.31) and (2.32) since it can be treated as system (2.28) considered previously (with ) when, and the corresponding solution is described by the formula (2.29).
The development of metal silver nanoparticles in aqueous solution was described by UV Vis spectroscopy.
The composition of nutrient solution was described by Chen et al. [ 18, 19].
Briefly, the equilibrium reactions between the electrode surface and the DA or dopamine- o-quinone (DOQ) in solution are described by where k1 and k2 are the adsorption rate constants of DA and DOQ, respectively, and k 1 and k 2 are the respective desorption rate constants.
The dependence of the specific degradation rate (q) on the initial styrene concentration in the solution was described by the Haldane equation, and the estimated constants of the equation were qm = 21 μg mgprotein−1 min−1, Ks = 7.5 μmol l−1 (0.78 mg l−1), and Ki = 0.215 μmol l−1 (0.02184 mg l−1).
The amount of HSA absorbed from the solution was described by mass balance using Equation (4): (4) A = C 0 − C × V m where A is the amount of HSA adsorbed onto PNBN-T (mg/g polymer); C0 and C are the concentrations of HSA in the initial (before adsorption) and final (after adsorption) solutions, respectively (mg/ml); V is the volume of the solution; and m is the mass of PNBN-T (g).
The behaviour of silver electrodes in AgNO3 solutions is described by an appropriate model.
Equation (10) has a regular singular point at (x=0), in which case the criterion for oscillatory solutions is described by inequality (5).
The CO2 absorption into the aqueous amine solutions is described by a combined mass transfer-reaction kinetics-equilibrium model, developed according to Higbie's penetration theory.
The CO2 absorption in the aqueous amine solutions is described by a combined mass transfer-reaction kinetics model developed according to Higbie's penetration theory.
