I think the question was about any pipe requiring complete drainage.
Per document EM 1110-1-4008, 5 May 99, pp.3-27 (internet pdf): "The elevation of the down-slope pipe support should be lower than the elevation of the lowest point of the sag in the pipe. This is determined by calculating the amount of sag and geometrically determining the difference in height required.
h = (L / n)^2 y / (0.25 (L / n)^2 - y^2)
where:
h = difference in elevation of span ends, mm, (in) L = span, m (ft) n = conversion factor, 10^-3 m / mm (1 ft / 12 in) y = deflection, mm (in) "
Ben
From: <a href="/group/PipingDesign/post?postID=zDsFRX0PGkHifJ-4oTYDhFyX5UGx2nUoGDyecp9EFpb4DFUybmlfIzqY6MGl5paCfYNcAvO1C0L3EN3ukNpHsV-7">PipingDesign@yahoogroups.com</a> [mailto:<a href="/group/PipingDesign/post?postID=zDsFRX0PGkHifJ-4oTYDhFyX5UGx2nUoGDyecp9EFpb4DFUybmlfIzqY6MGl5paCfYNcAvO1C0L3EN3ukNpHsV-7">PipingDesign@yahoogroups.com</a>] On
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Subject: Re: [PipingDesign] Slope in Steam lines
Hi,
Well it is not common to see Sloping steam line. May be it would have been
done in order to catch condensate. You can do away with slope if this is the
reason by intoducing drip legs and steam traps at low points. The drip legs
location should be at lowest point in that pocket and nos depend upon the
capacity required to remove the valuable condesate which in turn depends
upon primirarily on pressue (i.e L.P, M.P., H.P. and HHP).
Sloping lines have thier own problem so try not to see them on p&id`s untill and unless really warranted.
As to ur last qs I feel it is process designer responsibility to indicate any such reqt.
best regards
Hi all,
The Slope in steam lines is different (exp 0.5%, 1%, 2% <---- as I see in
some projects).
But Generally who should decide about the amount of slope (piping or process
designer) and how the suffiecient slope is calculated? does any criteria
exist to select the piping slope or related to experience?
Regards,
Mehdi Orojlu
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Received on Tue Jan 09 16:34:00 2007
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