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This is what is done with the formal system E, presented in Avigad et al. 2009.
Figure 2b, c, d, and e presented the images of the NiS/Gr-Ag CE at low and high magnifications.
In this study, we use the "probability of error reduction" p e presented in [54] to assess the differences in performance of the proposed weighting schemes.
The adsorption capacity of fluoride ions or amount of fluoride ions adsorbed (q e) presented in milligram per gram was determined using the following mass balance equation: q_{text{e}} = frac{{left( {C_{text{i}} - C_{text{f}} } right)V}}{m}, (2 where, C i and C f denoted the initial and equilibrium fluoride ion concentrations (mg/l), respectively.
Hemolysis between C1 to C2 and E presented variation in infusion pump A ranging from 0.503(± 0.740) in C1, 0.417(± 0.610) in C2 and to 1.131(± 1.180) in E. According to the studied infusion rates, hemolysis was higher to infusion pump A at 100 ml/h (p < 0.0001) and infusion pump B at 300 ml/h (p = 0.004).
As shown in Fig. 6c, device E presented a broad range spectrum with a CIE of (0.338, 0.372) and its spectrum curve almost fitted that of sunlight, exhibiting a spectra overlap ratio (the overlap area of the spectra between the WOLED and measured sunlight from 380 to 700 nm divide the integral area of sunlight) of 82.9 %, making it an appropriate candidate for sunlight-like illumination.
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Figure 3a and e presents an example of this analysis.
Figure 7d, e presents the FESEM images of sintered SiC pellet after addition of activated carbon.
Figure 6d, e presents the cross sections along the dark lines in Figure 6b, c, respectively.
Figure 6D, E presents the results weighted by Hamming and Chebyshev windows.
Figure 3d, e present the linewidth and normalized integral intensity maps, respectively.
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