Question 8.13: The velocity profile in the steady isothermal laminar flow o...

The velocity profile in the steady isothermal laminar flow of an incompressible Newtonian fluid contained between concentric cylinders in which the inner cylinder is rotating and the outer cylinder is stationary is given by

V=ωR12R22R12(R22xx) V =\frac{ωR_1^{2} }{R_2^{2}-R_1^{2}} (\frac{R_2^{2}}{x} – x)   for  R1xR2 R_1 ≤x≤R_2

where ω ω is the angular velocity of the inner cylinder, and xx is measured radially outward. Determine the rate of entropy production due to laminar viscous losses for SAE-40 engine oil at 20.0°C  in the gap between cylinders of radii 0.0500 and 0.0510 m when the inner cylinder is rotating at 1000. rev/min. The viscosity of the oil is 0.700 N·s/m² and the length of the cylinder is 0.100 m.

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First, draw a sketch of the system (Figure 8.14).

The unknown is the rate of entropy production due to laminar viscous losses. The material is SAE-40 engine oil at 20.0°C. Here, we use Eq. (7.72) for the viscous dissipation of mechanical work. By differentiating the velocity formula just given, we get

dVdx=ωR12R22R12(R22x2+1) \frac{dV}{dx} =- \frac{ωR_1^{2} }{R_2^{2}-R_1^{2}} (\frac{R_2^{2}}{{x^{2} } } + 1)

then

(σW)vis=μT(dVdx)2=ω2R14μ(R22R12)2T(R22x2+1)2(σ_W)_\text{vis}=\frac{μ}{T} (\frac{dV}{dx} )^{2} = \frac{ω^{2}R^{4}_1μ}{(R^{2}_2 – R^{2}_1)^{2}T} (\frac{R^{2}_2}{x^{2} }+1 )^{2}

Equation (7.69) gives the entropy production rate for viscous effects as

(S˙P)Wvis=V(σW)visdV(\dot{S} _P)_{\substack{\text{W}\\\text{vis}\\}}=\int_{\sout{V}}(σ_W)_\text{vis}d\sout{V}

For the differential volume element dVd\sout{V}, we use the volume of an annulus of thickness dxdx, or dV=2πLxdxd\sout{V} = 2πLx dx (Figure 8.15).

Putting these expressions for (σW)vis(σ_W)_\text{vis} and dVd\sout{V} into Eq. (7.70) and carrying out the integration gives

(SP)Wvis=2πLω2R14μ(R22R12)2T(2R22lnR2R1+R242R12R122)(S_P)_{\substack{\text{W}\\\text{vis}\\}} = \frac{2πLω^{2} R^{4}_1μ}{(R^{2}_2 – R^{2}_1)^{2}T} (2R^{2}_2\text{ln}\frac{R_2}{R_1}+\frac{R^{4}_2}{2R^{2}_1} – \frac{R^{2}_1}{2} )

where μ=0.700 N.s/m2,L=0.100 mμ = 0.700  \text{N.s/m}^{2} , \text{L}= 0.100  \text{m} , and

ω=(1000.revmin)(2π radrev)(1 min60 s)= 104.7 rad/sω = (1000.\frac{\text{rev}}{\text{min}})(\frac{2π  \text{rad}}{\text{rev}})(\frac{1  \text{min}}{60  \text{s}}) =  104.7  \text{rad/s}

R1=0.0500 m,R2=0.0510 mR_1 = 0.0500  \text{m}, R_2 = 0.0510  \text{m} , and T=20.0°=293.15 KT = 20.0°\text{C }= 293.15  \text{K}.

Substituting these values into the preceding formula gives

(S˙P)Wvis= 2.08 W/K(\dot{S} _P)_{\substack{\text{W}\\\text{vis}\\}}=  2.08  \text{W/K}

In this example, we have a reasonably high entropy production rate. This is due to the very small gap between the cylinders and the high viscosity of the engine oil. Check for yourself to see that (S˙P)W-vis0(\dot{S} _P)_\text{W-vis}→ 0 as R2R_2 becomes much larger than R1R_1, or as μ0μ → 0. Conversely, check to see that (S˙P)W-vis(\dot{S} _P)_\text{W-vis} → ∞ as R1R2R_1 → R_2 or as μμ → ∞ . Some of these elements are explored in the following exercises.

production rate (S˙P)(\dot{S} _P) vs. shaft angular velocity ωω as ωω varies from 0 to 10,000. rpm (Figure 8.16).
Answer: (S˙P) =133 W/K.(\dot{S} _P) = 133  \text{W/K.}

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