Exact(7)
The oxidation kinetics of the specimen showed parabolic behavior, indicating that the diffusion process prevailed during oxidation.
Electrochemical impedance showed a capacitive semi-circle and an apparent Warburg impedance, indicating that the diffusion process contributed to the total transfer rate.
By comparing the diffusion of pure methane and methane mixtures with the higher alkanes, it is observed that the diffusivity of methane is unaffected by the presence of the higher alkanes in the MOFs considered, indicating that the diffusion path of methane is not blocked by the higher alkanes present in natural gas.
For XC3, D/rc2 has almost the same value of 13X, indicating that the diffusion properties is similar for both cases, while the little bit smaller particle sizes for XC3 could make the breakthrough curve slightly steeper.
The plot (Fig. 4) of log (1 − F 2) versus t has yielded almost perfect linear curves for the removal of both As III) and As V) by TW/MnFe2O4 composite, respectively, but did not pass through the origin indicating that the diffusion of adsorbate into pores of the biosorbent was not the solely rate governing-step in both the cases.
A linear relationship was found for both free 5-FU aqueous solutions and 5-FU-loaded cubosomes with correlation coefficients of 0.985 and 0.992, respectively, indicating that the diffusion is the dominant mechanism of release.
Similar(53)
Results indicated that the diffusion of the larger epoxy molecule in polysulfone occurred more quickly when diffusing in the presence of the amine.
The results indicate that the diffusion of Cr into NiFe layer by annealing is uniform and hence a solid solution.
Investigations at thin-film level indicate that the diffusion caused by annealing is useful to form domain wall pinning sites.
The model predictions indicate that the diffusion step controlled the overall dissolution kinetics and is the rate controlling step.
Diffusion model analysis indicated that the diffusion coefficient of copper in iron was up to 0.63 × 10−14 m2/s during carbusintering process.
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