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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).
t payback = I initial C energy × E saving (15).
In step I, initial melting of the contacting surfaces is achieved at the amplitude bigger than the critical value.
Similar(15)
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).
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.
Where, D is the weight of dye (mg) in post hot wash or post cold wash liquor and D i = Initial dye weight in dye bath (mg).
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