Water Hammer in a Pipeline

2D twin of the 3D surge laboratory: a side view of the pipe, a pressure profile and live pressure traces, from the identical characteristics solver.

Presets

Playback

Pipeline

Closing the valve fast stops the water faster than the pipe can send the news upstream, so the pressure jumps by rho*a*v.

Valve

Model checks

The science

What is modelled

Water flows from a reservoir through a pipe to a valve. When the valve closes the moving water has to stop, the fluid compresses and the pipe walls stretch, and a pressure wave travels up the pipe at the wave speed a (about 1000 m/s in steel, much less in plastic). It reflects at the reservoir and comes back, so the pressure at the valve rings with period 4L/a.

Equations

  • Joukowsky: ΔH = a Δv / g, i.e. Δp = ρ a v for a closure faster than 2L/a.
  • Method of characteristics for the 1-D equations ∂H/∂t + (a²/g) ∂v/∂x = 0 and ∂v/∂t + g ∂H/∂x + f v|v|/(2D) = 0, solved along C± lines with time step dt = dx/a.
  • Valve: orifice law v = k(τ) √(2 g H) with a linear opening schedule; reservoir end: fixed head.
  • Slow closure estimate (Michaud): ΔH ≈ 2 L v / (g tc).

Checks run in the page

  • Near-instant closure against Joukowsky (5 %).
  • The duration of the pressure plateau against the round trip 2L/a.
  • A slow closure against the Michaud order of magnitude.

Each check builds a fresh, almost frictionless copy of the solver and compares it with the closed formula.

Honest simplifications

One-dimensional, quasi-steady friction, constant wave speed, no column separation or cavitation model (the page only flags negative head), no surge tank or air vessel, and a rigid linear valve schedule. Real design uses unsteady friction and cavitation models.

What to try
  • Press Sudden slam and watch the red pressure front run to the reservoir and back.
  • Raise the closure time above 2L/a (about 1.1 s here) and watch the peak on the right-hand graph fall.
  • Choose Soft plastic pipe: the wave is slower, the surge smaller, the ringing slower.
Pressure at the valve, mid-pipe and reservoir end
Pressure along the pipe: now, maximum and minimum
Flow velocity at the valve
Peak pressure against closure time
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