As depicted in Fig. P1.22, a spherical particle settling through a quiescent fluid is subject to three

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As depicted in Fig. P1.22, a spherical particle settling through a quiescent fluid is subject to three forces: the downward force of gravity (FG), and the upward forces of buoyancy (FB) and drag (FD). Both the gravity and buoyancy forces can be computed with Newton’s second law with the latter equal to the weight of the displaced fluid. For laminar flow, the drag force can be computed with Stokes’s law,

F= 3 π µ d ν

where µ  = the dynamic viscosity of the fluid (N s/m2), d = the particle diameter (m), and ν = the particle’s settling velocity (m/s). Note that the mass of the particle can be expressed as the product of the particle’s volume and density ps (kg/m3) and the mass of the displaced fluid can be computed as the product of the particle’s volume and the fluid’s density p (kg/m3). The volume of a sphere is πd3/6. In addition, laminar flow corresponds to the case where the dimensionless Reynolds number, Re, is less than 1, where Re = p d ν / µ.

(a) Use a force balance for the particle to develop the differential equation for dy/dt as a function of d, p, ps, and µ.

(b) At steady-state, use this equation to solve for the particle’s terminal velocity.

(c) Employ the result of (b) to compute the particle’s terminal velocity in m/s for a spherical silt particle settling in water: d = 10 mm, p = 1 g/cm3, ps = 2.65 g/cm3, and µ = 0.014 g/(cm∙s).

(d) Check whether flow is laminar.

(e) Use Euler’s method to compute the velocity from t = 0 to 2–15 s with Δt = 2–18 s given the parameters given previously along with the initial condition: ν (0) = 0.

As depicted in Fig. P1.22, a spherical particle settling through
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Numerical Methods for Engineers

ISBN: 978-9352602131

7th edition

Authors: Steven C. Chapra, Raymond P. Canale

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