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Pragma pipes

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For k = 0.40 [mm], water temperature t = 10°C, full profile<br />

Darcy-Weisbach/Colebrook-White Formula<br />

Quantity<br />

velocity<br />

hydraulic slope<br />

<strong>Pragma</strong> diameter [mm]<br />

9.5 Slopes and velocities of flow in PRAGMA ® <strong>pipes</strong> slopes<br />

The slope of the channel must also be<br />

considered as variable, since it is not<br />

necessarily completely defined by topo<br />

graphic conditions.<br />

The minimum channel slope is required<br />

to achieve the lowest flow velocity which<br />

will prevent suspended solids from settling<br />

out and clogging the pipe.<br />

In general, solid particles, e.g. sand particles,<br />

can deposit on the bottom to a<br />

depth corresponding to the particle friction<br />

angle (see Figure 9.1), expressed as<br />

where:<br />

hn – depth of flow, [m]<br />

d – inside pipe diameter, [m]<br />

Θ - internal friction angle, [°]<br />

If Θ = 35°<br />

then hn/d = 0,1<br />

The area of deposition may be allowed to<br />

a relatively flat zone of the channel bottom.<br />

Figure 9.1.<br />

Angle of friction<br />

The safe lower limit of velocity to avoid<br />

sedimentation depends on the type of<br />

sediments. Usually, the permissible minimum<br />

velocities (V sc ) which ensure selfcleaning<br />

of the channel should not be, at<br />

full flow, lower than:<br />

V sc = 0,8 m/s for sanitary sewers<br />

V sc = 0,6 m/s for storm sewers<br />

V sc = 1,0 m/s for combined sewers<br />

Pipelife<br />

www.pipelife.com<br />

24

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