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The microsieves are membranes for the experimental verification of filtration models.
One important parameter that is seldom considered explicitly in filtration models is the inter particle forces, e.g. electrostatic forces.
In principle, governing filtration models can facilitate the design of membrane processes than any experiment can, yet, experimentations are usually required for validation reasons (Peinemann et al. 2010).
Table 3 shows the overall summary of the results of filtration models when fitted to the experiments with the 5 kDa UF membrane at all TMPs.
Table 3 shows the coefficients of determination obtained from the filtration models when fitted to the experimental data with the 5 kDa UF membrane.
A mathematical relationship between these parameters and the specific deposit was established on the basis of saturated flow in soil equations, some filtration models and experimental results.
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Mudcake permeability cannot be measured directly, so it must be calculated with a filtration model, together with filtration data measured in the test which usually includes filtrate volume, filtration time, and pressure drop across the mudcake.
Brine was injected into the filtration model to determine the core permeability before filtration tests.
These results have application for screening level colloid filtration modeling of riverbank filtration in these systems.
The filtration model included a round tube withstanding a maximum pressure of 400 psi.
It means that isothermal filtration model will leads to underestimation of gas field potential.
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