To do this, you'll need to calculate your solute's molar mass and multiply it by the moles of your solute.
Simply add the molar masses of the solute's component elements to figure out the solute's molar mass.
To convert molarity to g/L, ppm, or percent composition, you'll need to convert the moles of your solute to a mass (using the molar mass of your solute compound).
Literature lacks on the simulation work on variation of concentration of solute for mass transfer rate and mass transfer efficiency in the complex system of bubble column device.
The model is corroborated against groundwater solute concentrations, mass loadings of solutes to the Arkansas River, relationships between solutes within the groundwater system, and overall regional statistics of groundwater solute concentration.
High flux (i.e. high solute concentrations) mass transfer in spherical, rigid drops has been studied for the case of a single transferring solute.
These properties form the often used "structural parameter", S, which accounts for a membrane's structural resistance to solute mass transfer within the support layer.
You already know the amount of solutes in grams, so convert by calculating (solute mass in grams) x ( 1 / molar mass ) to get the answer in moles.
The oxygen tension C r) [mol cm−3] in spherical coordinates was governed by the solute mass balance including Fick's law of diffusion, assuming (i) spherical symmetry, (ii) Michaelis Menten kinetics (Hiltmann and Lory, 1983), and (iii) steady-state: 1subject to boundary conditions: (∂ C/∂ r) = 0 for r = 0 (2andand C = C0 for r = rmax (2b).
Steady state diffusion of a chemical species in free solution can be described empirically using Fick's first law: vec{j} = - Dcdotvec{nabla }c (3)where (vec{j}) is the solute mass flux (in mol m−2 s−1); D is the diffusion coefficient of the solute in the solvent (in m2 s−1); c is the concentration of the solute in the solvent (in mol m−3).
