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ChemicalFluid FloweasyFE ExamCoursework

Reynolds Number for a Viscous Liquid

An oil with density ρ=900 kg/m3\rho = 900\ \text{kg/m}^3 and dynamic viscosity μ=2.0×103 Pa⋅s\mu = 2.0\times10^{-3}\ \text{Pa·s} flows at V=1.5 m/sV = 1.5\ \text{m/s} through a pipe of internal diameter D=50 mmD = 50\ \text{mm}.

Find the Reynolds number and state the flow regime.

Given
ρ900 kg/m^3Density
V1.5 m/sMean velocity
D50 mmInternal diameter
μ0.002 Pa*sDynamic viscosity
Hint 1

Reynolds number is the ratio of inertial to viscous forces.

Hint 2

Re = ρVD/μ, with all quantities in base SI.

Hint 3

Convert 50 mm to 0.05 m before substituting.

Worked solution — try the problem first

Re=ρVDμRe = \frac{\rho V D}{\mu}

Convert the diameter to metres — the only conversion needed:

D=50 mm=0.050 mD = 50\ \text{mm} = 0.050\ \text{m}

Re=900×1.5×0.0502.0×103=67.52.0×103=33,750Re = \frac{900 \times 1.5 \times 0.050}{2.0\times10^{-3}} = \frac{67.5}{2.0\times10^{-3}} = 33{,}750

Re=33,750 (turbulent)\boxed{Re = 33{,}750 \ \text{(turbulent)}}

Regime. For pipe flow, Re<2300Re < 2300 is laminar, 2300<Re<40002300 < Re < 4000 transitional, and Re>4000Re > 4000 turbulent. At 33,750 this is firmly turbulent.

Why it matters. The regime selects the correlation you may use — friction factor, heat transfer coefficient, mixing behaviour all change. Applying a laminar correlation such as f=64/Ref = 64/Re here would be badly wrong.

Reynolds number is dimensionless. If your working leaves units behind, an algebra error has crept in.

Concepts:Reynolds numberFlow regimesDimensionless groups

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