JouKowsky's formula is very commonly used as a basis and is quite useful as
a rough predictor. Ive found (as others ) reasonably reliable but it only
tells you one thing which is banally obvious anyway.
There's no easy way to do this properly. I've been to a number of courses specifically covering this topic and not got a straight answer yet. The best and most straightforward is Surge by the Don Wood UNiv Kentucky and a good and useful book <a href="http://www.engineer.ca/ASMENorthern/surge.htm">http://www.engineer.ca/ASMENorthern/surge.htm</a>
As always it involves buying and using his software.
NExt best is PArmakian but involves a lot of math and work.
After that theres a lot of other books of limited usefulness
Al
-----Original Message-----
From: Steve McKenzie [mailto:mechproj@xtra.co.nz]
Sent: Thursday, June 17, 2004 4:23 AM
To: <a href="/group/PipingDesign/post?postID=QG_gKhQsmyzsZ3U_5thYHaKuRShH2VSl-9qVoW0-R9VrpT_b3T1cniOdkPW6HWDNSNF9o5XWbLUBJF-6BxS69oByHQ">PipingDesign@yahoogroups.com</a>
Subject: [PipingDesign] Part full line - water hammer estimation
Gents + 1
I am looking at a water pipeline 2.8km long, flow rate 60l/s, ID
227mm.
The inlet is atmospheric from a tank. For the first 800m, the line
drops 150m in elevation. For the remaining 2km, the line is near
enough to horizontal, discharging into a pond. The friction loss
under full pipe conditions will be about 30m (dirty). This means that
the water will drop the first 120m (vertical) the line will run part
full, with fairly high velocities. At the -120m point the line will
become full with a fairly sharp head rise due to the sudden velocity
rise forming a sort of hydraulic jump. I can take a rough stab at the
part full velocity (using open channel flow theory) and I know the
full pipe velocity. To get the surge rise, I thought I may be able to
use Joukowsky's formula; delta H = a delta V /g; a is celerity.
However, I think the result will be overly conservative,and would
need to do a fair bit of work before being confident about the result.
This is a fairly common operating condition, but I do not seem to
have a clear estimation procedure for this.
Can anyone point me to a book or other reference?
Cheers
Steve
Yahoo! Groups Links Received on Thu Jun 17 11:59:00 2004
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