BEP Purely Geometric?
BEP Purely Geometric?
(OP)
My understanding of BEP is that it is based purely on geometry (and of course flow rate). Is this correct?
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RE: BEP Purely Geometric?
1.) the flowrate into the impeller closely matching the volume that the impeller's speed at the time and its "bite" can transfer to the discharge (geometry means nothing without considering speed).
2.) the friction of bearings and stuffings and seals
3.) the friction caused by the speed of the fluid moving through the pump.
4.) the recirculation from impeller discharge side, back to suction between impeller clearance space with casing
5.) the differential pressure between discharge and suction driving possible recirculation of fluid
Independent events are seldomly independent.
RE: BEP Purely Geometric?
Depending on the outlet triangle velocity and the diffuser geometry, the BEP can be estimated, but only confirmed after testing.
Operating at the BEP, the amount of recirculation would reach its minimum value
RE: BEP Purely Geometric?
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BEP Purely Geometric?
"1.) the flowrate into the impeller closely matching the volume that the impeller's speed at the time and its "bite" can transfer to the discharge (geometry means nothing without considering speed).
2.) the friction of bearings and stuffings and seals
4.) the recirculation from impeller discharge side, back to suction between impeller clearance space with casing"
RE: BEP Purely Geometric?
If you are discussing centrifugal pumps, be aware that all design is based on as is testing on pumping water at standard conditions, any other fluid requires the pump performance curve to be re-rated.
For more information I suggest you look on the internet, there will be a life-times reading available on anything you need to know, design, testing, re-rating, effects of temp., viscosity, atmospheric pressure, altitude, entrained air / solids, speed change, etc., etc.
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BEP Purely Geometric?
OK, thank you. The fact that centrifugal pumps are rated for, and tested with, water makes things make a lot more sense.
Just wondering though, if for instance, an EPC approached a pump manufacturer with a list of system specifications, would the pump manufacturer then go and re-rate (re-test) certain pumps to establish what would work best for that customers particular application? How do they incorporate the already esablished BEP into the specification when the customers specification does not match what they tested to in establishing that BEP?
RE: BEP Purely Geometric?
You're trying to establish why there is only one 'BEST' efficiency point for a pump? Probably because of the definition of the word 'best'.
BEP is the point at which a particular pump design is most efficient. It has nothing to do with what the customer wants, unless you are doing a custom pump design.
RE: BEP Purely Geometric?
AFAIK, there is no way other than to build a pump and test the hell out of it.
One part of the testing is to measure the pump's efficiency at a representative and exhaustive set of operating points.
From that data, a contour map can be generated and superimposed on the P-V curves that describe the pump's performance.
The BEP is within the highest measured efficiency contour.
Most pump manufacturers publish curve sets that include efficiency, so you can examine those contours for yourself.
There might be some possibly bizarre pump geometry that produces two or more loci of high efficiency, and there may be applications where that would be beneficial, but I haven't noticed such a pump yet. ... not that I spend any time examining pump curves when I don't have to.
Mike Halloran
Pembroke Pines, FL, USA
RE: BEP Purely Geometric?
What about pumps that are made for fluids with significantly different densities and viscosities than that of water (acids, emulsions, etc.). Those surely aren't benchmarked using water..?
RE: BEP Purely Geometric?
However, operation at BEP is not always at the top of the design goal list for real pumps in real systems.
Oh. Pumps for services other than water surely are benchmarked using water, because it's 'standard' and available at little cost in most locations. Corrections for other fluids are relatively simple to apply, and reproducible enough for most purposes.
To not answer your original question, it should be possible to generate a pump's curves solely from its geometry using CFD, but if anyone has actually done it, they're not talking about it, at least not loud enough for me to hear.
... and I don't expect it to happen real soon, because CFD is compute- intensive, and pump manufacture is basically a foundry operation, which is not compute- intensive.
Mike Halloran
Pembroke Pines, FL, USA
RE: BEP Purely Geometric?
Independent events are seldomly independent.
RE: BEP Purely Geometric?
If you change the gas inlet conditions then the you shift the map/curve.
During testing, Manufacturer build the performance database of the impellers using a standard gas. From that the curves are re-calculated for different/actual conditions using corrections (similitude laws and regression techniques). So for instance, when it happens that the real/actual gas and conditions used for prediction are close to the as-tested conditions, you will see immediately the manufacturer reduce their safety margin/tolerance on efficiency to gain some competitive edge.
Back to pump, BEP is nothing more, nothing less than a region of max efficiency in the iso-contour of the performance map. So the question of OP reads to me as follow do you shift the map/curve (up/down, left/right, rotate/steep) if you change the pumped liquid properties operating conditions by x,y % of course for a fixed impeller geometry/speed? I would say YES but needs someone to confirm.
I would add that the OP question is theoretical as in real world applications, before to notice some visible change in the curve/BEP (if any) you may have to change considerably your properties and operating conditions, that would already lead to issues upfront :
- Pump casing design parameters are limited (pressure, temperature)
- NPSH margin can be compromised
- Material selection of the pump is set for a specified medium
- All points mentioned by BigInch (bearing, sealing, recirculation, etc)
RE: BEP Purely Geometric?
Due to the generally varying range of flow rates, beside the peak efficiency (BEP), the shape of the efficiency curves is also considered an important factor when comparing expected pumps' performance.
RE: BEP Purely Geometric?
I would disagree with the statement that "a pump" only has one BEP. There are a lot of physical variables (impeller diameter, impeller mix, underfile, surface condition of hydraulic passages, case and impeller) that can affect the BEP of "a pump" while it is being manufactured. Even after manufacturing is complete and the pump configuration is now a constant* there are changes that can shift the BEP (running speed, impeller lift, correction factors for viscosity.) Now, with all things remaining constant, yes there is only one BEP.
*Never safe to assume that all things remain constant, bearing and wear ring clearances will deteriorate and there will be reductions in efficiency because of this. If you want a pump to have more than one BEP, run it for 10 years and then test it again.
No, it would be difficult to spec a pump with BEP matching that point during the design phase. It would be impossible to spec a pump that operates exactly at that point. Your system curve will not match the original design because everybody was conservative, so the pump will be oversized and run further left on the curve than anticipated.
RE: BEP Purely Geometric?
QUOTED ''factor water test data to actual fluid conditions.''
how do you do that in short if possible and then how this generally affects the curve (shape, shift, etc)?
tks
RE: BEP Purely Geometric?
The shutoff head (zero flow) is the same regardless of viscosity, but at increasing flow the curve "sags" more with viscosity (lower head due to head correction factor.)
BEP is shifted left due to the flow correction factor.
Power is increased at higher flows due to the efficiency correction factor.
For specific gravity changes:
Flow is unchanged
Head is unchanged (it is in units of distance (feet or meters) and not pressure so SG has no effect)
Power is adjusted by the ratio of specific gravity.
Pressure is adjusted by the ratio of specific gravity.
No change in curve shape
For speed changes or impeller diameter changes, see "affinity laws."
RE: BEP Purely Geometric?
Yep. Thanks.
RE: BEP Purely Geometric?
Unless you move to a non-newtonian fluid or a flow that is multi-phased then you can scale pump performance.
= = = = = = = = = = = = = = = = = = = =
Plymouth Tube
RE: BEP Purely Geometric?
RE: BEP Purely Geometric?
Also, in regards to 1gibson's statement:
"Here is how this works: start with fluid conditions (including one design point, one head one flow), select pump, review the preliminary curve, buy pump, test pump with water, factor water test data to actual fluid conditions and see if it is within testing tolerances, ship pump, install pump."
When you say: "test pumpt with water" why would you retest the pump? Hasn't the manufacturer already done extensive testing? Why would you buy the pump before seeing if the factored fluid conditions are within testing tolerances?
RE: BEP Purely Geometric?
Think you will find that most if not all pump manufactures will only guarantee pump efficiency on water under strict test conditions. Other liquors will be estimated only based on experience / tables etc. - the pump manufacturer has absolutely no control over application / installation / liquor properties. This becomes the responsibility of the end user.
It is a capital mistake to theorise before one has data. Insensibly one begins to twist facts to suit theories, instead of theories to suit facts. (Sherlock Holmes - A Scandal in Bohemia.)
RE: BEP Purely Geometric?
User - specify fluid conditions
Pump vendor - make preliminary pump selections (based on the actual fluid conditions) and quote to user
User - evaluate selections, pick one, purchase
Pump vendor - manufacture the pump, test with water, correct to actual fluid conditions, confirm it meets testing tolerances (confirm it passes test)
User - install and operate
Everything is on paper (or a computer) until the test results are in. Paragraph you quoted has nothing about a retest, the test is a test and that is why it is performed. It checks actual measured hydraulic performance vs the preliminary "on paper/software" information. It also confirms that vibration (and bearing temperatures when applicable) are acceptable.
RE: BEP Purely Geometric?