Sentence examples for i diffusion from inspiring English sources

Using this dimensionless number, three regimes of swelling kinetics can be identified: (i) diffusion is limiting, (ii) water uptake is limiting, or (iii) both processes are limiting.

We use now the model to study the sensitivity of the drug peak concentration and drug time-to-peak with respect to: (i) diffusion coefficients; (ii) clearance rates; (iii) membrane permeabilities; (iv) convective velocity.

It is also noted that the same mathematical formulation models: (i) diffusion through reverse-osmosis membranes; (ii) conduction through a partially insulated plate and (iii) potential flow through a series of plates.

Dynamic transfer process of P at DGT/sediment interface includes (i) diffusion flux and concentration gradients at DGT root)/porewater interface leading to porewater concentration (C0) depletion and (ii) P desorption from labile P pool in sediment solid to resupply C0 depletion.

The mechanisms by which O2 molecules are dissolved into the solution include (i) diffusion: Calculations using estimates of diffusion indicate O2 penetration distances in the pyrite sediment in the range of mm to cm (the uncertainties are high); (ii) evaporation-condensation.

This coupling gives rise to a number of interesting phenomena, such as an ion-size dependence of (i) diffusion coefficients of colloidal particles, and (ii) coagulation and deposition rates, interesting trajectories of tracer particles around large charged particles, an increase in viscosity and electrokinetic lift.

Starting from a given time t, the next event of reaction j in ν is according to Gillespie's algorithm (1976) at (1) Diffusion of species i with diffusion coefficient D i into another volume μ is translated into a first-order transport reactions with propensity a i = k i ν→ μ N i ν.

I measured diffusion in 6 locations, following Aβ1 42 diffusion for 705±145 ms, during which time the width of the Gaussian fit increased from 6.5±1.0 µm to 13.7±2.46 µm.

Where t is the lag time, τ i the diffusion time of the ith diffusing species, and ρ i the contribution of ith species.

Modeling of mass uptake is presented in terms of Case I (Fickian diffusion) and Case II (kinetic) models.

These are the limits of (i) oxygen diffusion control, (ii) proton conductivity control, and (iii) mixture control.