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how often do I need an air release valve
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11 Mar 04 20:16
I am installing a new pipe line and would like to incorporate air release valves into the system. The problem is I don't know how often I need these valves. If anyone knows of a formula or book or website or anything that has this information it would be very helpful. Thanks in advance.
(Nuclear)
beerginger,I'm a bit confused here. You wanted to know "how often you need these valves." Are you meaningIf your question is the latter, then it's somewhat easy: the valves go at the high points in the installed piping; one valve to each high point.
Patricia Lougheed
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(Mechanical)
Well said by VPL. If your piping is open ended liquid piping, you may require none. If it is a closed loop piping then you have to install them at the highest point. A thermostatic trap is a good air vent incase of steam piping.Regards,
Eng-Tips.com : Solving your problems before you get them.
(Mechanical)
Check out valmatic or ventomat websites . Thye have software for designing the system with location and type of air valves required. The Ventomat site has some other good technical information on air valves.Be carreful as some older styles of air valves can actually cause pressure transients. The Ventomat is designed specifically to mitigate surges in a system.
(Mechanical)
stanier, that Vent-O-Mat link was good, have some good looking products and technical papers.
PUMPDESIGNER
(Civil/Environmental)
VPL has given you the answer -you need one valve at each high point. That is if you have a main transmission pipeline. If you have a distribution pipeline with connections then generally you can allow the pipe to vent through connections and you don't need air valves. Air valves need maintenance.
For a main pipeline you also need to ensure that the air moves to the air valve. Typically pipes should be laid at a minimum gradient of 1 in 500 when rising to an air valve and 1 in 500 when falling from an air valve.
On long lengths you may also need air valves at changes in gradient - generally spacing should not exceed 1 to 1.5 km.
Having decided where to locate the vales you will need to decide what size to make them. There are three requirements
1) to vent large volumes of air during filling
2) to allow air into the pipe during emptying (some pipe materials can collapse under negative pressure i the pipe is drained faster than the valve will admit air into the pipe.
3) to vent small volumes of air that come out of solution during service.
To cater for these requirements it is common to use double orifice air valves that contain a large orifice to allow air evacuation and air entry during filling and emptying and a small orifice that allows venting of air accumulation during service.
To size the air valves you need to consider the filling rate and the rate that the air will need to be evacuated during filling. If you have a pipe material that is susceptible to collapse under vacuum you will also need to consider the maximum drain down rate and the rate you need to allow air into the pipeline to limit the sub atmospheric pressures.
The Vent-o-Mat design guides will give you the methodology but beware Vent-o-mat are in the business of selling their valves and if you follow their guides you will end up with larger valves than some of us would consider necessary.
.
(Mechanical)
Pumpdesigner has come back with some good information.I would add another need for air valves and open a complex subject in doing so. Air valves can be used to mitigate pressure transients resulting from loss of power pump stop. Computer modelling will show that a large air valve may in fact cause higher pressure transients than a smaller orifice valve. This works against you when you select an air volve to exhaust large volumes of air. Hence the double orifice type valve. Large orifice to exhaust the air and small orifice when the approaching air water interface is close to the air valve.It is this latter scenario that resulted in the research for the Ventomat style of Kinetic double air valve.In respect of the size and number of air valves I agree that the Ventomat software rpedicts more and larger valves than necessary. the local Ventomat representative in Australia, AVK valves, acknowledges this and will work with you to review a design. I have also come across this problem with Valmatic's selection software.It must be remebered that air valve suppliers are not design consultants receiving fees for the design engineering of a system. So there may well be some conservatism in their software. I agree with Pumpdesigner that you need to understand the theory , research and application of air valves. Thier misapplication is as serious as for a relief valve! Typically unforeseen pressure transients could compromise the thrust blocks in a pipeline, will result in long term fatigue damage of pump seals, bearings, valve seats, instrumentation etc.A read of Fluid Pressure Transients in Pipelines by ARD Thorley is worthy of your time. It is out of print at the moment but any good technical library or authority should have a copy.My conclusion is that the technology of ball type kinetic valves has gone the way of 8mm filmimg, DOS, Video 8, black & white TV and other legacy products. There are better designed valves out there. Yes they do cost more up front but they prove to save money by their reduced maintenance and reduction in risk for your pipeline.Also sit the air valve on a short branch on a blind flange fitted to a full size tee to allow a point where the air can accumulate and egress from the system.
(Civil/Environmental)
Using air valves to relieve surge pressures is a contentious subject for potable water pipelines.
There are two problems:
1) on initial pipeline filing the large orifice air valve of a double orifice vlve will slam closed as water reaches the ball. This will set up a transient pressure in the pipeline. If analysis shows this to be a problem then you need to send more on a slow closing air valve. Vent-0-mat is one option.
2)During service if there is power failure causing a sudden pump trip and the resultant negative pressure wave causes pressures in the pipeline to go subatmospheric air will be drawn into the pipeline. This air will then be expelled under the subsequent positive pressure wave. Sudden closure of the air valve will cause secondary pressure waves which when combined with the initial pressure waves may lead to rupture of the pipe.
The argument for using slow closing valves such as Vent-o-mat is that allowing air into the pipeline provides a cushion which reduces the waterhammer pressure wave. Because the air is subsequently expelled slowly through the slow closing valve there are no adverse secondary transient pressures. However, for potable water few authorities will permit a design that allows pipeline pressures to fall below atmospheric. The concern is that any polluted water that is sitting in the air valve chamber may be drawn into the pipeline. There is also concern that if a pipeline is subject to subatmospheric pressure polluted water may be drawn into the pipeline through spigot and socket joints. For this reason the Vent-o-mat arguments have not found a great deal of support in the water industry.
It is unusual for excessive surge pressures to compromise thrust blocks. Thrust blocks are usually designed for test pressure plus a nominal factor of safety and as such have adequate factors of safety to resist surge pressures. Furthermore shock loading from surge pressures is usually too short lived to mobilise failure of the thrust block. The main failures I have observed are longitudinal splitting of pipes, collapse of pipes and flange failure.
However, this is straying from the argument - I would say that there are many good ball type air valves on the market - don't get too hung up on the Vent-o-mat sales talk and paying for air valves you don't need.
(Mechanical)
The message from BRIS makes some good points in relation to air valves. I would like to extend the discussion as it is fleshing out some misconceptions on these devices.1) Filling of pipelines should always be done slowly, in a controlled manner, to ensure that htere is no damage to air valves and other devices in the system. It would be foolhardy to rely upon the Ventomat or any other air valve to prevent that.2) The problem of air, water or pollutant ingress into potable water lines exists because there are already air valves designed into potable water lines. This has been argued as necessary to prevent air restricting the capacity of the pipeline. If one looks at a crude oil, petroleum or slurry pipeline there are no such devices? Is it a myth? I dont think so because there are many reported instances of air in the line causing hydraulic restrictions. Then why dont other industry pipelines suffer from the same problem?Yes, one has to be wary of sales talk in engineering matters. However Ventomat are able to back up their point of view with independent research. Many of the ball type air valve manufacturers have copied a design and have no idea of the way a kinetic air valve works. The original kinetic air
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