OpenFlows | Water Infrastructure Forum - Surge Tank Headloss Coefficient
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Question

Surge Tank Headloss Coefficient

by
Bentley Communities Legacy Member
Expert

Hello good morning;

I am modeling a surge tank to protect a pipe for transient event.

When I dont consider headloss coefficient ( Headloss coefficient = 0) tthe system works normally but when I consider a headloss coefficient different to 0 (always positive), HAMMMER dont compute. 

image

Additional Surge Tank input data:

  • Operating Range type: elevation
  • Elevation (Base): 726.91
  • Elevation (Minimum): 726.91
  • Elevation initial:731
  • Elevation (Maximum):734

  • Elevation (physical): 726.46
  • Volume(inactive): 0
  • Section: Circular
  • Diameter (m): 0.10 (it is a 4" stand pipe)
  • Treat as Juction: True

  • Surge Tank Type: Simple
  • Has check valve: False
  • Weir coefficient:1.84
  • Weir Length: 0.5 m
  • Diamter orifice (mm): 100
  • Ratios of losses:2.5
  • Headloss coefficient: ?

  • The pipe is a 450 mm diameter ductil Iron (lenght 6100m) with a flow of 100 l/s 
  • Reservoir elevation: 731.23m
  • Valve close time:120 seg.

Where do you think is the error? Maybe the little diameter of the onlet and surge tank (4"=0.1m = 100mm) 

Thank you very much for your support

Kind regards.