set to terminate computations in the event of a pipe collapse. Where
the buckling limit is below the gas release level then the formation of
gas- or vapour-filled cavities will inhibit any further fall in head and
so internal pressure should not reach the level at which buckling occurs.
22.9.2 Descending outfall
The second example considers an idealised outfall similar to one of the
case studied by Larsen (1976). The pipeline descends uniformly over a
distance of 3 km. Pumping is used to overcome resistance with the
suction well level set at þ0.0 mAD. The pipeline is at 30.0 mAD at
its discharge point. An initial uniform eccentricity of 2% was adopted.
Gas release was represented and the pipeline was without lateral
support. After pump trip the minimum head shown in Fig. 22.9 was
predicted. The damping effect shown is essentially due to the pipe flex-
ibility as positive internal pressures preclude gas release. Appreciable
damping of the pressure wave is also evident in this figure.
If the pipeline is supported by stiffeners, flexibility is reduced. After
trip, the minimum head along the main falls to a greater extent than
before, as shown in Fig. 22.10. Greater amplitude of head variation
also occurs than without supports, again indicating a smaller amount
of damping in this stiffer pipeline.
Chaina
e (m)
Series 1
Series 2
Series 3
Descending flexible pipeline. con = 6, del/D = 2%, h
b
= 12.3, gas c = 0.000 01
Elevation (mAD)
0
100
200
300
400
500
600
700
800
900
1000
1100
1200
1300
1400
1500
1600
1700
1800
1900
2000
2100
2200
2300
2400
2500
2600
2700
2800
2900
3000
40
30
20
10
0
–10
–20
–30
Fig. 22.9. Envelope curves for descending outfall after pump failure and 2%
deflection ratio
Flexible pipe