Fluid Mechanics, HVAC & Refrigeration · Pipe wall and surge
The wall, and the hammer
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The wall, and the hammer

Two relations, and they only mean anything side by side: one says what a pipe can hold, the other says what the water will throw at it.

Barlow's formula, P=2StDP = \dfrac{2 S t}{D}P equals two S t over D. PP is the internal pressure the wall can contain, SS is the hoop stress the material is allowed to carry (its yield strength divided by a code safety factor), tt is the wall thickness and DD the outside diameter. Keep tt and DD in the same unit and their ratio is bare, so the answer comes out wearing whatever unit SS wore — MPa in, MPa out. The 2 is not decoration: it comes from balancing the pressure across a diameter against two wall sections, one on each side. Read the shape of it and the trade lore falls out — thicker wall, proportionally more pressure; bigger bore, proportionally less. That is why large mains are the expensive ones.

Joukowsky's equation, ΔP=ρaΔv\Delta P = \rho\, a\, \Delta vdelta-P equals rho a delta-v. ΔP\Delta P is the surge pressure ABOVE line pressure in pascals, ρ\rho the fluid density in kg/m³, Δv\Delta v the velocity destroyed in m/s, and aa the wave celerity — the speed the pressure wave travels back up the pipe, roughly 1200–1400 m/s in steel, but only 300–500 m/s in thermoplastic, because a plastic wall stretches as the wave passes and takes the edge off it.

Look at what is NOT in that equation: the length of the pipe, and the pressure already in it. Length decides only whether the closure counts as sudden; the peak itself does not care. And the surge rides on top of whatever the line was carrying — the wall feels the sum, which is exactly the sum a verdict has to be made against.

Run the numbers once and the fear becomes useful. Water at 2 m/s in steel, stopped dead: 1000×1200×2=2.4 MPa1000 \times 1200 \times 2 = 2.4\ \mathrm{MPa}, which is 24 bar of surge on a line that may never see 4 bar in service. A quarter-turn ball valve closed by an enthusiastic apprentice does this. The three remedies are slower closure, a surge vessel, and lower velocity — and only the last one is free, because it was a sizing decision all along.