I'm not sure if this post is appropriate, but I just had to ask.
Does anyone have an idea of what this multi-branch 'teelateral' would be for (assuming it's not a joke)?
I'd have called it an octo-tee or something, but there appears to be more than eight branches.
http://www.pipingdesign.com/paulin_research_group_visit.html
These photos were taken at Paulin Research Group in Houston a few years ago.
Does anyone know how many Markl machines are in existence?
Paul
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SPED Calgary
http://calgary.spedweb.com
Piping Design Central...
The below is copied from an article written by Gordon Reddek for Piping Design Central. I've been unable to contact Mr Reddek for a few years.
http://www.pipingdesign.com/eccentric_reducers.html
What are your comments on his thoughts about the correct orientation of FOB/FOT?
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As you...
In areas that have risk of damage from, uh, let's say, ballistic violence or non-internal pressure-induced explosions, why aren't the lines buried?
Is it a cost factor?
It would seem to me that technology advances in trenching would make this more economical especially if combined with sensors...
I'm not sure if this is appropriate for this forum but it sure is an impressive set of photos of a refinery under construction:
http://www.pipingdesign.com/images/reliance_refinery.pdf
"Reliance Industries plans to complete its ambitious $5.7
billion expansion of Jamnagar Refinery Project...
What is the difference between these terms on a P&ID:
-Free draining
-No pockets
-Slope
All of these refer to the concept of preventing (via piping
configuration) liquid build-up (possibly due to condensation) downstream
of the safety valve in order to avoid backpressure on the PSV spring...
RE: thread378-24153 (now closed)
A member of my piping design discussion group mentioned today that copies of the Datalog are available for US$50 from:
http://www.basicpsa.com/navco_piping_datalog.htm
I hope this doesn't sound like an ad (I have no affiliation with the seller) as my...
For steam service, bottom flat reducers upstream of control valves are recommended to minimize the possible accumulation of condensate and sediment.
Is the same configuration preferred for other fluids as well?
One other reason for FOB (flat on bottom) reducers in control stations with up and...
Jacques Chaurette's (of Fluidedesign.com) pump FAQ is at:<br><br><A HREF="http://www.fluidedesign.com/s61.htm" TARGET="_new">http://www.fluidedesign.com/s61.htm</A><br><br>It is definitely worth a look.<br><br>[if the above link fails to function, go to <A HREF="http://www.fluidedesign.com"...