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The experimental result of the initially fluidized granular flow has three distinct regimes: (i) initial acceleration, (ii) constant velocity, and (iii) stopping (see Roche et al. 2008 for details).
(i) Initial reachability matrix .
x o (i) : Initial particles are randomly generated.
W i: initial weight (g) A: surface area (m2).
where b is the Langmuir isotherm constant, C i initial fluoride concentration (mg/L).
All these aspects, specific to PHWRs, also lead to management of large quantities of: (i) initial fuel (ii) irradiated fuel, and (iii) radioactive wastes.
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This gave us a model f-I initial slope of 0.432, a final slope of 0.099, and a rheobase of ~0 pA (see Figure 2).
This gave us a model f-I initial slope of 0.136, a final slope of 0.089, and a rheobase of 5 pA (see purple solid and dashed lines in Figure 4).
The decolorization efficiency of the isolate was expressed as per following equation: (1) Decolorization % = I − F / I Where, I = Initial absorbance (Control) and F = Absorbance of decolorized medium broth.
C i = Initial concentration of phenol (mg L−1).
Where, D i = Initial dye weight in dye bath (mg) and D pdl = dye weight (mg) in post dye liquor.
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