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Stan’s Legacy The Stanley Meyer Archive

Pressure drop round the loop

What pressure does it take to push the medium round the loop at this speed, and what hydraulic power is that?

The formula
Δp=f⁢LD+K⁢ρ⁢v22
Δp
Pressure drop, Pa
f
Darcy friction factor
L
Loop length, m
D
Bore, m
K
Sum of minor-loss coefficients
ρ
Medium density, kg/m³
v
Mean velocity, m/s
LaTeX
Δp = \left( f \cdot \frac{L}{D} + K \right) \cdot \frac{ρ \cdot \left( v \right)^2}{2}

Work it out

kg/m³

Density of the slurry or gas as a whole.

mPa·s

Dynamic viscosity of the medium.

in/s

Mean speed along the tube. The EPG #1 holding specifies 50 in/s for slurry.

mm

Inside diameter of the tube.

m

Total length of tube the medium travels in one lap.

The sum of the loss coefficients for everything that is not straight tube: about 0.3 per smooth bend, 1 per sharp elbow, 1–2 for a pump housing, 0.5 for each sudden contraction.

Method

  1. Find the Reynolds number, ρ·v·D ÷ η.
  2. Choose the friction factor by regime: 64 ÷ Re below 2300 (Poiseuille — the loss is proportional to velocity); Blasius's 0.316·Re^−¼ above 4000 (the loss goes nearly as the velocity squared), or Haaland's smooth-pipe form above Re = 10⁵; a straight line between the two across the transition band.
  3. The dynamic pressure is ρ·v² ÷ 2. The straight run costs f·L ÷ D of it and the bends, fittings and pump housing cost K of it; add the two and multiply.
  4. The flow rate is the velocity times the bore's area, π·D² ÷ 4. Pressure times flow rate is power: the hydraulic work the pump does on the fluid each second, before the pump's own efficiency — a small centrifugal pump turns perhaps a fifth of its shaft power into this.

Assumptions

  • A smooth tube: glass, acrylic or drawn metal. Roughness raises the turbulent friction factor and Haaland's full form takes it; a rubber hose or a cast fitting can be half again as lossy.
  • A Newtonian medium. A slurry above about ten per cent solids, or any magnetised slurry inside the coil, has a yield stress and a shear-thinning viscosity that this cannot follow; the pressure drop is then a floor.
  • The minor-loss coefficients are handbook values for water in ordinary fittings. The loss in a coil-wound section, where the bore may step, is the reader's to estimate.
  • Nothing here is Meyer's except the velocity the EPG #1 holding specifies and the pump rating it gives. Darcy–Weisbach is nineteenth-century hydraulics, and the friction factors are Poiseuille's and Blasius's.