Is cracking pressure a pressure drop?
Is cracking pressure a pressure drop?
(OP)
On a check valve... is cracking pressure something to take into consideration when adding up pressure drops? Thanks!
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Is cracking pressure a pressure drop?
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RE: Is cracking pressure a pressure drop?
There's a good article on check valves at the spirax website.
Cheers,
K
RE: Is cracking pressure a pressure drop?
So I just need the Cv factor? the 5 or 10 psi cracking pressure really doesnt have much to do with anything but getting the valve open...
RE: Is cracking pressure a pressure drop?
It's my understanding that if you relate this to a mechanical system, such as a cart, the cracking pressure would be the same as the static friction. They resist up until the point where the system starts moving. The pressure drop across the valve, once it has opened, would be the equivalent to the kinetic friction of the cart.
You may want to read up on sizing check valves. Check valves that are improperly sized can do all kinds of bad things to themselves. For instance a check valve that is too large will "chatter" and can become damaged.
Cheers,
K
RE: Is cracking pressure a pressure drop?
RE: Is cracking pressure a pressure drop?
I don't think that you are correct. The way I learned it, dP opens the valve and fluid momentum keeps it open. A 2-inch check valve takes about 0.5 psid to open and I've never measured anything close to 0.5 psi pressure drop across one that was open.
kacarrol's analogy to static and sliding friction is exactly the way that I've always thought of it.
David
RE: Is cracking pressure a pressure drop?
RE: Is cracking pressure a pressure drop?
David
RE: Is cracking pressure a pressure drop?
Fluid momentum keeping the valve open results in a pressure drop.
RE: Is cracking pressure a pressure drop?
You can, theoretically, sink below the cracking pressure and still have the valve leaking a little bit of fluid. That's where the reseal pressure comes into play.
http://www.j-pascal.jp/image/B5D5BBDFCADBSPCV.pdf
But for pressure drop calculations, I stick to my original statement, use the Cv of the valve to calculate that and make sure that your check valve is sized properly to stay open when needed and reseal when needed.
RE: Is cracking pressure a pressure drop?
But. I have digital pressure gauges that are advertised to have a repeatable uncertainty of 0.01 psig and in the 2 dozen times I've put them before and after a check valve in a flowing stream they always show a 0.00 dP. So I'm thinking that the pressure lost in the momentum transfer is in the microbar range. Not zero, but not measurable with field instruments.
On the other hand the purpose of the exercise has been to quantify cracking pressure (trying to understand performance of wellbore deliquification techniques), and those numbers are very much measurable on a field gauge (and no, simple calculation of dP times gate area is not very close to actual cracking pressure, it seems like there is always a non-zero adhesive force holding the valve closed, not sure why, but it is always there).
David
RE: Is cracking pressure a pressure drop?
dPtotal= Pc + SG * (Q/Cv)2
BTW, Smith Valves shows Cv for swing check valves which are substantially higher than even their globe valves,
http://
These swing-checks don't show an opening, or cracking pressure, probably because in most systems the downstream head would be many magnitudes greater than that anyway and it really wouldn't matter.
In a counterbalanced swing check, initially the differential pressure x the Sin(swing_angle)- the counterbalance weight x cos of the counterbalance angle would have to be greater than zero to open. As soon as flow began, the initial static differential pressure would decrease from the Bernoulli effect, as that static pressure converts to velocity head. Its not the static pressure vs the velocity head, or one or the other, its the sum of both that works to keep the swing plate open. Then the valve would remain open when flowing only when the sum of upstream pressure plus velocity head impacting the angled surface (from the vertical) of the swing-plate, V^2/2/g * Sin(α) plus any frictional drag effects on the plate remains greater than the counterbalance force x the Cosine of its angle (measured from horizontal) - any downstream backpressure.
So, the "cracking pressure" is really the static head equivalent of the energy required to open the swing with no flow, which then becomes the sum, if you will, of all forces, pressure, drag and velocity impact forces acting on the plate, I think more appropriately should be called what, "the total differential head across the valve".
"The top of the organisation doesn't listen sufficiently to what the bottom is saying." Tony Hayward X-CEO BP
http://www.youtube.com/watch?v=hpiIWMWWVco
"Being GREEN isn't easy." Kermit
http://virtualpipeline.spaces.live.com
RE: Is cracking pressure a pressure drop?
We've had the discussion about the difference between head and pressure over and over again, and it is just too subtle for my tiny brain. I can measure pressure. Most descriptions of measuring "head" read just like what I do to measure pressure. OK, call it "cracking head", but that sounds like something a Chicago cop does on a Saturday night. But yes, what seems to be called "cracking pressure" is at zero flow.
My contention is that (just like static friction vs. sliding friction) some non-trivial amount of dP is required to open the conduit to allow flow to begin, then the required dP to keep the conduit open becomes vanishingly small. Not zero, but very small. In my mind your equation that adds the cracking pressure to a momentum term is nonsense. It should be:
dPtotal=Ppost-cracking + SG*(Q/Cv)2
Even with reasonably high velocities (the highest I've done this on is Mach 0.25 in a 4-inch line), the dP across a check valve and 12-inches of pipe has been less than I could measure. As I said, on the order of micro-bars. There's no doubt that it is there, it just isn't a very large number.
The original question was "On a check valve... is cracking pressure something to take into consideration when adding up pressure drops?". I still say no.
David
RE: Is cracking pressure a pressure drop?
The other "word equation" is a Bernoulli type,
z1 + ρ1/γ1 + v12/2/g - Hl =
z2 + ρ2/γ2 + v22/2/g
It works for any two points within or across the valve.
Some of the velocity head is converted to pressure as it stagnates when it impacts the plate, and some of the available pressure is used to reaccelerate it so that gpm in = gpm out; net result is pressure drop.
Evidence abounds for pressure drops for check valves. Hard to believe its all wrong.
http://www.engvalves.com/itemfiles/fabrif10.pdf
"The top of the organisation doesn't listen sufficiently to what the bottom is saying." Tony Hayward X-CEO BP
http://www.youtube.com/watch?v=hpiIWMWWVco
"Being GREEN isn't easy." Kermit
http://virtualpipeline.spaces.live.com
RE: Is cracking pressure a pressure drop?
0.1 to 1 psi at various flowrates for 6" to 60" valve sizes
http:
"The top of the organisation doesn't listen sufficiently to what the bottom is saying." Tony Hayward X-CEO BP
http://www.youtube.com/watch?v=hpiIWMWWVco
"Being GREEN isn't easy." Kermit
http://virtualpipeline.spaces.live.com
RE: Is cracking pressure a pressure drop?
If you extrapolate the graph to the 2-inch, 3-inch, and 4-inch valves that I did my tests on, and extend the lines down to the 200-600 MSCF that was normal flow for most of the tests that I did, you get a vanishingly small dP. Not zero, but pretty low.
Nothing I've said contridicts the references that you've provided. I've not said that past research is wrong. I have said that at the flows that I normally experience, I've never had instruments sensitive enough to measure the flowing dP. I never said that they weren't there, I just said they were too small for field instruments to see.
The difference between the equation I took exception to and my minor rewrite is that I took your Pc to be cracking pressure. My (clarification? refinement? meddling?) was to clarify that there is a dP required to initiate flow (cracking pressure or head) and a different, lower dP once flow starts. The OP is asking if you have to add cracking pressure to the system head, and I still contend that you don't.
David
RE: Is cracking pressure a pressure drop?
http:/
and here,
Pct of Full Open Cv vs Pct Full Open of Disc,
also shows my aerodynamic analogy is appropriate,
http
The link provided by kacarrol, for checks specifically noted as having a cracking pressure, says it adds, so do I in the case where there is a spring,
http://www.j-pascal.jp/image/B5D5BBDFCADBSPCV.pdf
Flowserve's chart on page 5 shows the difference for a spring and a no-spring valve, where static pressure is converted to momentum, the cracking pressure decreases, as the valve opens, then increases again once reaching full open,
http://ww
Note that it doesn't go away, the pressure drop is Pc + SG * (Q/Cv)^2, however Pc is variable due to the conversion of static pressure to kinetic flow as the valve opens.
You've motivated me to try to do a CFD for an opening swing check valve to see if it matches the Flowserve chart showing that variable Pc reduces, as pressure drops when the fluid accelerates (according to a Bernoulli venturi type prediction), opens the disc and dP begins increasing again. I have this very strong feeling that it will.
"The top of the organisation doesn't listen sufficiently to what the bottom is saying." Tony Hayward X-CEO BP
http://www.youtube.com/watch?v=hpiIWMWWVco
"Being GREEN isn't easy." Kermit
http://virtualpipeline.spaces.live.com
RE: Is cracking pressure a pressure drop?
David
RE: Is cracking pressure a pressure drop?
"The top of the organisation doesn't listen sufficiently to what the bottom is saying." Tony Hayward X-CEO BP
http://www.youtube.com/watch?v=hpiIWMWWVco
"Being GREEN isn't easy." Kermit
http://virtualpipeline.spaces.live.com
RE: Is cracking pressure a pressure drop?
RE: Is cracking pressure a pressure drop?
My only problem with your equation was that I took it to imply that whatever dP was required to open the check valve would be present in the flowing system. My experience has been that dP builds up to initiate flow and drops off to a vanishingly small number. Adding a multi-psi cracking pressure to "less than measurable" dP would overstate system dP.
Robster1us,
"Check valves" are one of those ubiquitous pieces of equipment that we don't think about much. In my mind a "check valve" is a "swing check valve" and all my knowledge that says that is only one of many types doesn't stop me from thinking that a check is a check. I've seen the same blind spot about ball valves. We still don't know what the OP was asking about or if he has answers to his questions.
I've been kind of argumentative in this thread, primarily because the concept of "magnitude" keeps getting lost in fluids engineering. When I go through the methods in Crane 410 and add up the additional pipe lengths for fittings and valves, I get a number. If I take that pipe length into a gas flow equation like the AGA Fully Turbulent equation, I get about the same number as if I hadn't bothered to account for the fittings. It is different, but I've never had it lead me to a different decision. And that is what is important any any mathematical modeling. The magnitude of the effects just doesn't change my decision. It is useful to be as "rigorous" as possible, but once you've reached that point you get a number. Then you have to look at that number and see how it effects your decision. A microbar dP across a gravity check valve just doesn't push me to a different pipe size.
David
RE: Is cracking pressure a pressure drop?
I was told that the valve has to keep oil from leaking into a boiler, and there is about 25' of 1/2"ID vertical pipe above where the valve will be and then after the valve there is an oil burner... so I guess I will have to get a valve with a spring to give me a higher cracking pressure to overcome the static head...
I guess they want a valve to keep the lines primed with oil, but without having to install any actuators or anything else but a check valve in each line
Thanks a lot for all your help
RE: Is cracking pressure a pressure drop?
http://ww
Understanding the full impacts of check valves in the line is proabably a whole bunch easier if you've had to fix an undersized pump suction line where somebody forgot to include 1 km of length.
"The top of the organisation doesn't listen sufficiently to what the bottom is saying." Tony Hayward X-CEO BP
http://www.youtube.com/watch?v=hpiIWMWWVco
"Being GREEN isn't easy." Kermit
http://virtualpipeline.spaces.live.com
RE: Is cracking pressure a pressure drop?
RE: Is cracking pressure a pressure drop?
The OP's use of the valve is completely different than its designed use.
Correct me if I'm wrong but a 'spring' in a spring loaded check valve is to assist in the reseating, not to be used as a regulating device.
The arguement between BigInch and David is semantical at the sizes we're talking about. Forest for the trees.
Whether its a loss in static head or velocity head is immaterial....the spring requires a constant force to be overcome therefore it needs to be accounted for.
I have to say using a spring check as an actuating device is not very appropriate in my opinion.
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Tomorrow is another one.
Every day, from here to there,
funny things are everywhere. ~'Dr.' Theodor Geisel
RE: Is cracking pressure a pressure drop?
The problem is that the customer does not want to run any pneumatic or electric and manual is out of the question.... so the check valve was all I could think of...
Is there another option that I may be unaware of?
RE: Is cracking pressure a pressure drop?
RE: Is cracking pressure a pressure drop?