Properties of Fluids: Worked Examples

These examples progress from basic property conversions to viscous shear, interfacial effects, compressibility, cavitation checks, and ideal-gas applications. Intermediate values retain sufficient precision before final rounding.

Density, Specific Weight, Specific Volume, and Specific Gravity

A reservoir contains 825 kg825\ \text{kg} of oil in 0.917 m30.917\ \text{m}^3. Determine its density, specific weight, specific volume, and specific gravity. Use g=9.81 m/s2g=9.81\ \text{m/s}^2 and ρw=1000 kg/m3\rho_w=1000\ \text{kg/m}^3.

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Dynamic and Kinematic Viscosity

A lubricating oil has dynamic viscosity μ=0.290 Pa⋅s\mu=0.290\ \text{Pa·s} and density ρ=850 kg/m3\rho=850\ \text{kg/m}^3. Determine its kinematic viscosity in m2/s\text{m}^2/\text{s}, stokes, and centistokes.

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Viscous Force and Power between Parallel Plates

A plate of area 1.50 m21.50\ \text{m}^2 moves at 0.400 m/s0.400\ \text{m/s} over a stationary plate. A 0.150 mm0.150\ \text{mm} layer of castor oil separates them, with μ=0.981 Pa⋅s\mu=0.981\ \text{Pa·s}. Assuming steady Newtonian flow and a linear velocity profile, determine shear stress, resisting force, and required power.

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Capillary Rise in Water and Depression in Mercury

A clean glass tube has inside diameter 2.50 mm2.50\ \text{mm}. Determine the capillary change for (a) water with σ=0.0725 N/m\sigma=0.0725\ \text{N/m} and θ=0∘\theta=0^\circ, and (b) mercury with σ=0.520 N/m\sigma=0.520\ \text{N/m}, SG=13.6SG=13.6, and θ=130∘\theta=130^\circ. Use γw=9810 N/m3\gamma_w=9810\ \text{N/m}^3.

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Excess Pressure in a Droplet and Soap Bubble

A water droplet and a soap bubble each have diameter 2.00 mm2.00\ \text{mm}. Take σ=0.0720 N/m\sigma=0.0720\ \text{N/m}. Determine the excess internal pressure in each.

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Excess Pressure in a Cylindrical Liquid Jet

A cylindrical water jet has diameter 4.00 mm4.00\ \text{mm} and surface tension σ=0.0720 N/m\sigma=0.0720\ \text{N/m}. Neglecting axial curvature, determine the pressure inside the jet relative to the surrounding gas.

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Bulk Modulus from a Small Compression Test

A liquid volume decreases from 1000 cm31000\ \text{cm}^3 at 1.00 MPa1.00\ \text{MPa} to 995 cm3995\ \text{cm}^3 at 2.00 MPa2.00\ \text{MPa}. Estimate the average bulk modulus over this interval using the initial volume as the reference.

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Volume Change from a Known Bulk Modulus

A chamber initially contains 3.00 m33.00\ \text{m}^3 of water. Pressure increases by 5.00 MPa5.00\ \text{MPa}. Estimate the volume decrease using K=2.20 GPaK=2.20\ \text{GPa} and treating KK as constant over the interval.

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Density and Specific Weight of Air

Air is at 150 kPa150\ \text{kPa} absolute and 30.0∘C30.0^\circ\text{C}. Determine density and specific weight using R=287 J/(kg⋅K)R=287\ \text{J/(kg·K)} and g=9.81 m/s2g=9.81\ \text{m/s}^2.

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Absolute Pressure and Cavitation Check

Water at 20.0∘C20.0^\circ\text{C} flows through a suction line where a gage reads −100.0 kPa-100.0\ \text{kPa}. Local atmospheric pressure is 101.3 kPa101.3\ \text{kPa} and water vapor pressure is 2.34 kPa2.34\ \text{kPa} absolute. Determine the local absolute pressure and assess whether a single-phase liquid state is sustainable.

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Ideal-Gas Bulk Modulus for Two Compression Processes

Air is at 200 kPa200\ \text{kPa} absolute. Estimate its bulk modulus for (a) isothermal compression and (b) reversible adiabatic compression with k=1.40k=1.40.

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