Pigging or Flushing a 15 km Non-Uniform Pipeline

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Guidance is sought for cleaning a 15 km non-uniform pipeline with alternating 4" and 6" sections, facing a pressure loss of approximately 30 bar at a flow velocity of 1 m/s. The pipeline lacks vent points, raising concerns about air displacement during flushing and pigging operations. The discussion includes evaluating pigging options, such as dual-diameter pigs, and flushing setups to manage air effectively. Additionally, there are inquiries about pump requirements to maintain the necessary pressure head for the pipeline configuration. The conversation highlights the challenges of cleaning without pig traps and the implications of the pipeline's design on cleaning methods.
Finchh
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Hello all,

I’m looking for some guidance on cleaning a 15 km non-uniform pipeline that alternates between 4" and 6" Schedule 80 sections, with reducers, bends, and a non-barred tee section (P&ID attached for reference). We’ve calculated a total pressure loss of approximately 30 bar at a flow velocity of 1 m/s, accounting for friction, bends, and head loss. There are no vent points available, so air displacement is a concern for both flushing and pigging operations.

Pipeline Details:​

  • Length: 15 km
  • Diameters: Alternating 4" and 6" Schedule 80 sections
  • Pressure Loss: Around 30 bar at 1 m/s flow velocity
  • Tee Section: Non-barred tee included in the line
  • Vent Points: None available
Given the diameter transitions and the non-barred tee section, I’m evaluating both pigging and flushing options. If anyone has insights on handling non-uniform lines with tees in terms of pig selection (such as dual-diameter or adaptable pigs) or advice on flushing setups to manage air displacement without vent points, I’d appreciate it. Additionally, any suggestions on pump requirements to consistently achieve the 30 bar head for this configuration would be extremely helpful.

Thanks in advance for your input!
6 & 4 inch line.png
 
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I have no experience with pigging, but does it work with such small diameter pipes and varying diameters like this? (not to mention such tight turns)
 
My idea is that I want to use immerse Whitetail Antlers in a fishtank to measure their volumetric displacement (the Boone and Crockett system is the current record measurement standard to place in a juxtaposition with) I would use some sight glass plumbed into the side of the tank to get the change in height so that I can multiply by the tank cross-section. Simple Idea. But... Is there a simple mechanical way to amplify the height in the sight glass to increase measurement precision...

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