Control volume and section averages
Identify inlets, outlets, and impermeable walls of a fixed region. A is area normal to flow; v is section-average normal speed. Uniform profiles let these speeds represent streamline velocities.
Check yourself: Is there an uncounted branch, leak, or accumulation inside the region?
Continuity
Steady single-inlet, single-outlet flow requires ρ₁A₁v₁ = ρ₂A₂v₂. At equal constant density, A₁v₁ = A₂v₂ = Qᵥ. A smaller area increases speed at fixed volume flow, not mass flow.
Check yourself: Did you justify canceling density before equating volume flow rates?
Bernoulli assumptions
For steady incompressible inviscid flow along one streamline, with gravity and no machinery energy exchange, p + ρv²/2 + ρgz is constant. Using section averages without a kinetic-energy correction additionally assumes uniform velocity profiles at those sections.
Check yourself: Can friction, a pump, or different streamlines invalidate your comparison?
Pressure datum and elevation
Use a common pressure datum and elevation origin. Gauge pressures can share the same atmospheric reference because only their difference enters. Cancel elevation terms only for equal elevations.
Check yourself: Does a pressure decrease supply increased kinetic energy, elevation, or both?
Limits of the ideal model
Neglecting viscosity removes wall friction and dissipation, but not every liquid flow is lossless. Nonuniform profiles and losses require a fuller energy balance. Constant temperature keeps the liquid-property model fixed here.
Check yourself: Which missing physical effect would require an additional term?