Govt. Exams
Entrance Exams
Modern pump design standards recommend 20-30% safety margin above NPSH_required to ensure cavitation-free operation
Settling velocity = 0.02 m/min = 1.2 m/h. Overflow rate = 1 m³/m²·h means rise velocity = 1 m/h < 1.2 m/h, so particles will settle
Re = Vx/ν; 5×10⁵ = 10×x/(2×10⁻⁵); x = 1.0 m
Optimal Venturi throat diameter ratio is typically 2.5-3.0 for smooth operation and minimal vibration
Fr = 1 defines critical flow; Fr < 1 is subcritical; Fr > 1 is supercritical
Cavitation occurs when available NPSH is less than required NPSH, causing vapor bubble formation
In isothermal compressible flow with friction, pressure decreases while velocity increases due to fluid expansion
Rotameter float position equilibrium depends on drag force, buoyancy, and weight - all affected by fluid viscosity and density
For sharp-edged orifices, discharge coefficient typically ranges from 0.60-0.65, with 0.61 being standard for β = 0.6
For sudden expansion, Cp = 1 - (A₁/A₂)² = 1 - (D₁/D₂)⁴ = 1 - (0.05/0.1)⁴ = 0.9375, but accounting for losses, recovery coefficient ≈ 0.56