Figure 2b presents the corresponding logarithmic removal value (LRV), calculated as . Note that in Figure 2a,b, the time axis is logarithmic and that for convenience, AZD5582 cell line it was normalized by the time t 1/2 defined by the condition (half-saturation time). The agreement of these numerical results with the measured filtration performance reported in [5, 6] is fairly good. In particular, we obtain an initial LRV of 6.5 log, equal to the LRV measured in [5, 6] when the actual filters

(composed by a macroscopic array of microchannels) were challenged with only about 1 L of water (the authors of [5, 6] estimate that such volume carries a total amount of impurities that is orders of selleck screening library magnitude smaller than the total available binding centers in their filter, so the measurement is expected to correspond to almost clean channels, as in fact seems to be confirmed by microscopy images [5]). The calculated LRV is of 4 VX-680 log at t/t 1/2≃0.7,

which is also in fair agreement with the observation of a 4 log filtration in [5, 6] after passing through the macroscopic filter approximately from 200 to 1,000 L, depending on the measurement. However, obviously, a more stringent determination of the parameter values, and in general of the degree of validity of our equations, would need more precise and detailed data. Unfortunately, to our knowledge, no measurements exist for the time evolution of the filtering efficiency of channels with nanostructured walls with a t-density

and precision sufficient for a fully unambiguous quantitative comparison with the corresponding STK38 results of our equations; in fact, one of the main motivations of the present Nano Idea Letter is to propose (see our conclusions) that such measurements should be made, in order to further clarify the mechanism behind the enhanced impurity trapping capability of the channels with nanostructured inner walls. As a further test, we have repeated the same numerical integration as in Figure 2a,b but considering a radial impurity concentration profile , instead of a constant one as in Equation 4. We have obtained very similar results, provided that the parameter Ω1 z 0 is conveniently varied: In particular, we observed that the filtration dynamics results obtained using Equation 4 and any given value γ for Ω1 z 0 can be reproduced using the above Debye-like profile if employing for Ω1 z 0 a new value (specifically, the new value can be estimated, by comparing the initial filtration performance, as , where ; for instance, taking , which probably is a fair first approximation for the measurements in [5–8], the parameter values used in Figure 2 correspond to 3.2 × 104/m as equivalent Ω1 z 0 value when using the Debye approach).