Cheers,
sanjib basu <basusan2000@yahoo.com> wrote:
Dear Piping Designers/Pipeliners,
The excellent clarity of advise on Pig launcher/ receiver Gordon Rededek again reissued by Paul makes me sit up and feel that probably i could get real help & advise on the problem below:
I have a LPG Pipeline 6" x 30 Km which is to be pigged while commissioning.
The Procedure what is to be adopted may be:
1.Pig the line dry after Hydrotest with HD Foam pig till the foam is touch dry.
2. Introduce Nitrogen Slug between two pigs with say 30% volume/length of the
pipeline
3.Introduce LPG ( pressure available 21 BarG) behind the second Pig
4.Blow out the air & Nitrogen by opening two block valves installed back to back
by crack opening First & then fully open second procedure.. out of Receiver
connected to a separate Vent line erected at a safe distance & height.
5. When Liquid LPG comes in behind the Second Pig --- What should I do?
Supposing I discharge some in atmosphere & close the valves by following the reverse procedure and Close the mainline valve at the receiver, how do I remove the liquid in the Scrapper Trap?
Drain it? Where? how? Safely?
The Client wants to do a baseline survey with LPG and hopes to do it say at an interval of 4 years to asses Corrosion/ pitting if any. At that time the scrapper on either side will be full with Liquid LPG... how do we safely dispose it.
Any one who worked in the Operation please advise. I will have further questions to ask about venting too from TRV's.
Sanjib Basu
[Non-text portions of this message have been removed]
[Non-text portions of this message have been removed]
Received on Sat Jul 28 18:22:00 2007
This archive was generated by hypermail 2.1.8 : Mon Oct 27 2008 - 20:24:12 EDT