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Oil flow between fixed plates problem

Short answer

Using pressure gradient 4000 Pa/m, u_max = h^2|dp/dx|/(8μ) = 0.417 m/s; Q = (h^3|dp/dx|/(12μ))×b = 2.78 L/s; ū = 0.278 m/s; τ_w = (h/2)|dp/dx| = 20 Pa; u(2.5 mm) = 0.3125 m/s; h_f = Δp/(ρg) = 2.27 m; Re = 20.8, laminar.

Oil of viscosity 0.12 Pa s and specific gravity 0.9 flows steadily in laminar motion between two fixed horizontal parallel plates 10 mm apart. The pressure drops by 20 kPa over a length of 5 m. For a plate width of 1 m, find (a) the maximum velocity, (b) the discharge, (c) the mean velocity, (d) the shear stress at the wall, (e) the velocity at 2.5 mm from a plate, (f) the head loss over 5 m, and check that the flow is laminar.

Given data

μ=0.12 Pa s\mu = 0.12\ \text{Pa s}, ρ=900 kg/m3\rho = 900\ \text{kg/m}^3, h=0.01 mh = 0.01\ \text{m}, L=5 mL = 5\ \text{m}, Δp=20 000 Pa\Delta p = 20\,000\ \text{Pa}, b=1 mb = 1\ \text{m}.

Pressure gradient magnitude: ∣dpdx∣=20 0005=4000 Pa/m\left|\dfrac{dp}{dx}\right| = \dfrac{20\,000}{5} = 4000\ \text{Pa/m}

(a) Maximum velocity

umax=h28μ∣dpdx∣=(0.01)2×40008×0.12=0.4167 m/su_{max} = \frac{h^2}{8\mu}\left|\frac{dp}{dx}\right| = \frac{(0.01)^2 \times 4000}{8 \times 0.12} = 0.4167\ \text{m/s}

(b) Discharge

Per unit width:

q=h312μ∣dpdx∣=(0.01)3×400012×0.12=2.778×10−3 m2/sq = \frac{h^3}{12\mu}\left|\frac{dp}{dx}\right| = \frac{(0.01)^3 \times 4000}{12 \times 0.12} = 2.778\times10^{-3}\ \text{m}^2/\text{s}

For b=1 mb = 1\ \text{m}: Q=2.778×10−3 m3/s=2.78 L/sQ = 2.778\times10^{-3}\ \text{m}^3/\text{s} = 2.78\ \text{L/s}.

(c) Mean velocity

uˉ=qh=2.778×10−30.01=0.2778 m/s(=23umax)\bar u = \frac{q}{h} = \frac{2.778\times10^{-3}}{0.01} = 0.2778\ \text{m/s} \quad (= \tfrac23 u_{max})

(d) Wall shear stress

τw=h2∣dpdx∣=0.005×4000=20 Pa\tau_w = \frac{h}{2}\left|\frac{dp}{dx}\right| = 0.005 \times 4000 = 20\ \text{Pa}

(e) Velocity at y=2.5 mmy = 2.5\ \text{mm}

u=12μ∣dpdx∣(hy−y2)=40000.24(0.01×0.0025−0.00252)=0.3125 m/su = \frac{1}{2\mu}\left|\frac{dp}{dx}\right|(hy - y^2) = \frac{4000}{0.24}\left(0.01 \times 0.0025 - 0.0025^2\right) = 0.3125\ \text{m/s}

(f) Head loss

hf=Δpρg=20 000900×9.81=2.27 m of oilh_f = \frac{\Delta p}{\rho g} = \frac{20\,000}{900 \times 9.81} = 2.27\ \text{m of oil}

Check for laminar flow

Taking the plate gap as the characteristic length:

Re=ρuˉhμ=900×0.2778×0.010.12=20.8≪2000Re = \frac{\rho \bar u h}{\mu} = \frac{900 \times 0.2778 \times 0.01}{0.12} = 20.8 \ll 2000

So the flow is laminar.

Answer: umax=0.417 m/su_{max} = 0.417\ \text{m/s}, Q=2.78 L/sQ = 2.78\ \text{L/s}, uˉ=0.278 m/s\bar u = 0.278\ \text{m/s}, τw=20 Pa\tau_w = 20\ \text{Pa}, u(2.5 mm)=0.3125 m/su(2.5\ \text{mm}) = 0.3125\ \text{m/s}, hf=2.27 mh_f = 2.27\ \text{m}

✓ Answer checked by Claude Opus 5.5 (high effort)

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