NPSH Margin in Vertical Turbine Pumps
NPSH Margin in Vertical Turbine Pumps
(OP)
I'm doing a design review for a seawater system using vertical turbine pumps in located in sumps within tanks. The system is to be designed to pump the capacity of the tanks in 9 hours. To do that requires 5000 gpm to be pumped. The BEP of the selected pumps is 3800 to 4000 gpm, but the builder determined early on (before I became involved) that it was possible to operate these pumps at the end point of the curve until we identified possible NPSH constraints as the tank levels decreased. Their solution was to install VFD's, but slowing down the pumps blew the time constraints. The builder then proposed increasing the maximum speed of the pumps 200 rpm to gain a minor amount of additional capacity on the high end.
In order to run the pumps at maximum capacity (to meet the 9 hour constraint) the NPSH margins being used in their simulation are almost non-existent - in the neighborhood of 1 to 3 %. ANSI/HI 9.6.1-1998 states that "NPSH margins are not normally a consideration for most standard vertical turbine pumps, since they generally have a Low Suction Energy and cavitation noise is not an issue." I calculate a suction specific speed of 12,800, but to tell the truth, based on what I've read, I'm not clear on whether this makes it high energy or low.
I would prefer a 5000 gpm pump operating at BEP. Then we wouldn't be looking at NPSH. The situation is complicated by fact that the pumps have been purchased and delivered. I would like an NPSH margin ratio of 1.2 to 1.3 and minimum of 5' (based on Hydraulic Institute recommendations), but I will admit that this amounts to a factor of safety because I'm not sure of what I'm dealing with when operating so far outside "normal" parameters. I'm not sure sure how to intelligently determine what NPSH margin is required without expensive, detailed analyses that might be required only due to a poor selection of pumps. I can't seem to get the attention of the builder with my technical concerns.
My concern is obviously for the longevity of the pumps. I'm not sure what indications of cavitation will be available to the operators with these pumps when located 55' down in a tank (other than loss of discharge pressure). Unless something similar to Goulds PumpSmartĀ® in installed, I think the pumps will be routinely operated in cavitation.
There may be many things I've gotten wrong here. NPSH is not something I generally need to get involved with and have little experience with the finer details. I'd appreciate any input you guys might be able to provide. Thank you.
In order to run the pumps at maximum capacity (to meet the 9 hour constraint) the NPSH margins being used in their simulation are almost non-existent - in the neighborhood of 1 to 3 %. ANSI/HI 9.6.1-1998 states that "NPSH margins are not normally a consideration for most standard vertical turbine pumps, since they generally have a Low Suction Energy and cavitation noise is not an issue." I calculate a suction specific speed of 12,800, but to tell the truth, based on what I've read, I'm not clear on whether this makes it high energy or low.
I would prefer a 5000 gpm pump operating at BEP. Then we wouldn't be looking at NPSH. The situation is complicated by fact that the pumps have been purchased and delivered. I would like an NPSH margin ratio of 1.2 to 1.3 and minimum of 5' (based on Hydraulic Institute recommendations), but I will admit that this amounts to a factor of safety because I'm not sure of what I'm dealing with when operating so far outside "normal" parameters. I'm not sure sure how to intelligently determine what NPSH margin is required without expensive, detailed analyses that might be required only due to a poor selection of pumps. I can't seem to get the attention of the builder with my technical concerns.
My concern is obviously for the longevity of the pumps. I'm not sure what indications of cavitation will be available to the operators with these pumps when located 55' down in a tank (other than loss of discharge pressure). Unless something similar to Goulds PumpSmartĀ® in installed, I think the pumps will be routinely operated in cavitation.
There may be many things I've gotten wrong here. NPSH is not something I generally need to get involved with and have little experience with the finer details. I'd appreciate any input you guys might be able to provide. Thank you.





RE: NPSH Margin in Vertical Turbine Pumps
The higher the specific speed, the more NPSH is usually required. You don't mention the rpm now, but an increase to 200 rpm isn't very high, but depends more on the percentage over the original design speed.
I would suggest, if changing the pumps is not practical, that you approach the problem by evaluating the validity of the time constraints and increase the allowed time if possible. Also the time that these pumps will be running at marginal NPSH might not be very long, so see if those ideas might give you some reasonable alternatives to rejecting the existing pumps.
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RE: NPSH Margin in Vertical Turbine Pumps
http://www.gouldspumps.com/pag_0007.html
RE: NPSH Margin in Vertical Turbine Pumps
I was looking for advice on NPSH margins using the existing pumps. Solid NPSH requirements will preclude the use of these pumps. They can't use them and meet the 9 hour requirement unless they operate at no margin. I feel a margin is necessary, particularly given the unknowns. I know they're the wrong pumps. I'm looking for unshakeable arguments to get rid of them when getting rid of them is going to cost the other party big dollars. If anybody has input regarding necessary NPSH margin, I'd appreciate it.
RE: NPSH Margin in Vertical Turbine Pumps
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RE: NPSH Margin in Vertical Turbine Pumps
What has Flowserve had to say about operating at end of curve, at the end of the day they are the ones to consult with for clarification.
RE: NPSH Margin in Vertical Turbine Pumps
I agree that it might not be clear exactly where the pumps will actually operate. Our SimSmart model indicates they will operate somewhere close to the end points. There's not a lot of backpressure.
The Flowserve rep is the one who initially recommended and is supporting their continued use under these conditions. My feeling is he probably didn't have a 5000 gpm pump so he sold what he had. This isn't the only instance of an inappropriate pump, just the worst one. There's no way this pump should have been considered.
I'm usually pretty good at finding my way past the sales reps to get in touch with technical people, but I haven't had any luck getting contact information for anybody other than sales reps at Flowserve. I don't know how to get past the guy who is representing Flowserve to us. That rep has no problems with the intended operating points. He's the one who suggested increasing the speed of the pumps and said we could operate right up to the NPSHr curve before any cavitation occured. That's just patently false. I don't know what his qualifications are, but how do you question someone's credentials and wind up with any cooperation at all? I'm just at my wit's end. I don't know how to decisively shut this subject down. Everything I've read points to - like you said - BIG problems.
RE: NPSH Margin in Vertical Turbine Pumps
Gary Bakke, Customer Service Engineer
Phillipsburg, NJ
Tel: 908-859-7049
Email: gbakke@flowserve.com
Brook Campbell, Application Engineer
Houston, TX 77008
Tel: 713-803-4438
Email:
RE: NPSH Margin in Vertical Turbine Pumps
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"We can't solve problems by using the same kind of thinking we used when we created them." -Albert Einstein
RE: NPSH Margin in Vertical Turbine Pumps
Another reference is Cavitation and the Centrifugal Pump Aguide for Pump USers. Another resource is www.mcnallyinstitute.com
RE: NPSH Margin in Vertical Turbine Pumps
I agree that you need to get to someone other than a sales rep. so that you can get this sorted out.
RE: NPSH Margin in Vertical Turbine Pumps
I don't think I'm blaming the pump company rep for anything other than recommending - what I consider - the wrong pump to a builder that didn't know better. I don't think a person well-versed in the technical issues would consider this a good fit for the application. The rep has been active in supporting the continued use of these pumps. Who then is responsible? The builder ultimately, but they are being supported by the person who recommended and sold them the pumps. He's not suggesting that this is a poor application. Not even close.
All I'd really like is to know what NPSH margins Flowserve might think these pumps need to operate successfully over time. I don't think I'm getting qualified information from the only company person I have available to me. If they're not the proper source of information for their product, who is? Seriously, I don't know who to ask.
If the builder can technically support the operation of the pumps as presently intended, I'll listen. At this point, I haven't received any real technical support for this operation other than the fact that the only contact the builder has at Flowserve is saying that they can operate with almost no margin and that it won't be a problem.
With enough NPSH margin, I tend to agree. So the question to me comes down to a difference of opinion as to how much margin is required. The face of Flowserve says operation up to the NPSHr value is acceptable. I'm certain that's not correct, but I don't know exactly what a good number is. The question in my mind is still - how to determine a reasonable NPSH margin for the operation of these vertical turbine pumps. With enough margin, these pumps won't make 9 hours, but they will operate successfully. That's the whole point.
RE: NPSH Margin in Vertical Turbine Pumps
I have been in the situation (unfortunately) several times as a project engineer for large food processing companies. I would:
Ask Flowserve to guarantee the performance and operation over the range of operating conditions of the pumps. If they won't do that I would put the builder on notice that the system is not properly designed. You then have the option of paying for the changes yourself (if you feel unplanned failure will cost more than replacing it now) and suing the builder for breach of contract OR waiting until they fail.
You can also hire an independent engineer (perhaps one with the joint approval of the builder) to examine the system and determine if it has been properly designed. You can then proceed based upon his recommendation.
Either of the above will help you in case of a lawsuit later. In the food processing industry we really could not tolerate unplanned (major) downtime and there were several times when we changed the design. We would give the contractor additional money for the incremental cost of the better equipment but nothing for returns or demolition of work that was already done. Usually the contractor and the supplier worked things out so that there was as little monetary loss as possible since both wanted to continue working at the facility.
RE: NPSH Margin in Vertical Turbine Pumps
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RE: NPSH Margin in Vertical Turbine Pumps
Following are good centrifugal pump selection criteria:
NPSH margin = 4 feet minimum
Suction Specific Speed, Nss = 11,000 maximum
Rated Capacity = 80% to 110% BEP
Curve Stability = continuously rising to shutoff
Head Rise to Shutoff = 10% minimum t0 20% maximum
Installed / Max Impeller Diameter = 95% Maximum
Maximum HP at runout= 95% Motor Nameplate rating
Nss of your pump is 12800 which indicates that it could have maintenance (bearing, seal life)issues in the future due to internal recirculation at the impeller eye
RE: NPSH Margin in Vertical Turbine Pumps
Extending the time is the biggest no brainer available. If that wasn't the first solution considered, I'd have to be an idiot.
RE: NPSH Margin in Vertical Turbine Pumps
http://turbolab.tamu.edu/pubs/Pump21/P21pg018.pdf is a good read. I'd found that before and was one of the indicators that we might have a problem.
What I've read indicates that there is a problem with recirculation at the impeller eye only with flows below that of BEP - in the neighborhood of 50%. An interesting issue, but another subject I think.
I understand that operation at zero margin is not always a problem and doesn't have to be a problem, but we're not operating at BEP or even 110% of BEP. We're at 150% of BEP. My problem is that I don't know and don't have the experience to operate outside normal operating parameters. The greater the deviation from established guidelines, the more attention has to be paid to the details. It doesn't mean you can't go there - you just have to know what you're doing. If we were at BEP or close to it, I wouldn't even have raised the issue.
I appreciate the input and the support, guys. Thanks a lot.
RE: NPSH Margin in Vertical Turbine Pumps
NPSH calculation are made with absolute pressure not gage pressure. Atmospheric pressure is part of NPSHa. A vertical wet pit sump pump has 14.7 PSIA, 34 feet water column NPSHA to begin with from atmospheric pressure acting on the water surface. To the 34 feet, you add the static head from the water surface to the eye of the first impeller. If you have 4 feet of submergence, NPSHa is 34' + 4' = 38'
NPSHr can not exceed NPSHa. If it does, the pumping system will be a failure resulting from poor design.
Ask Flowserve for a performance curve drawn at the VFD speed they propose. Require the 12 month warrantee.
RE: NPSH Margin in Vertical Turbine Pumps
RE: NPSH Margin in Vertical Turbine Pumps
Wishful thinking or looking for someone to say "yes you have enough NPSH margin" will not overcome the poor pump selection.
As you are responsible for a design review and not getting any response from your client to your concerns re the poor pump selection, prepare your report based on your concerns of poor selection and the long term viabilty of the pump units, the assurance of the Flowserve rep that the pumps will operate as required and your job is complete, present it and your job is completed. You cannot be responsible for other peoples assurances / mistakes or your clients inabilty to be concerned with your findings.
RE: NPSH Margin in Vertical Turbine Pumps
I know they aren't calculating for enough margin, but how can you say they don't have enough NPSH margin if you can't say what that margin should be? Okay, how do I say that? That's why I'm here. That's the only reason I'm here asking questions. I'm looking for something to hang my hat on and I see the NPSH argument as the strongest at this point. I can say I'm concerned about the margin, I can say I think with the unknowns involved that there should be more margin, I can say that ANSI/HI 9.6.1 recommends this or that margin, but if I can't say what the margin should be be with some authority, it weakens the argument immeasurably. This argument would have been easier to win if there weren't expensive, already purchased 55' long pumps involved. The train left the station a long time ago.
I'm trying to get the builder to face what I consider to be the facts. Until they agree with me that those are the facts, we don't move forward. They seem to be convinced in the face of everything that these will operate acceptably. I don't understand it, but further agreement without technical justification won't help persuade them.
I've goten some good tips though and I appreciate all the input.
RE: NPSH Margin in Vertical Turbine Pumps
Besides NPSHa/r margins there are other factors to be considered, you also need to consider the operation so far out on the curve where pre-rotation, internal recirc etc are likely to be encountered, deflection of impeller and shaft and insufficient submergence likely to entrain air due to vortexing of the incoming flow plus the very poor hydraulic efficiency which equates to $$$ and can cost a fortune over the life of the pumps.
I realise you are in a bind - caught between supplier and owner - but you can only present what you have along with your recommendations, it's the owners final choice which way to go on this.
RE: NPSH Margin in Vertical Turbine Pumps
I regress in stating my initial comment. Either change the pump, or change the operation spec to allow a longer pump out time and you might as well slow your flowrate down to the pump's BEP while you're at it. Those are the only ways to make it right. For some reason it appears that you just can't make the decision, so pass it along to someone who has the authority or economic interest to do so.
http://virtualpipeline.spaces.msn.com
"We can't solve problems by using the same kind of thinking we used when we created them." -Albert Einstein
RE: NPSH Margin in Vertical Turbine Pumps
RE: NPSH Margin in Vertical Turbine Pumps
http://virtualpipeline.spaces.msn.com
"We can't solve problems by using the same kind of thinking we used when we created them." -Albert Einstein
RE: NPSH Margin in Vertical Turbine Pumps
RE: NPSH Margin in Vertical Turbine Pumps
RE: NPSH Margin in Vertical Turbine Pumps
http://virtualpipeline.spaces.msn.com
"We can't solve problems by using the same kind of thinking we used when we created them." -Albert Einstein
RE: NPSH Margin in Vertical Turbine Pumps
I never thought these were the correct pumps and have told the ship owner - the one who's paying for the ship. That these pumps have not been properly selected according to standard practice was and is obvious. The mfg. recommended the pump for operation at the endpoint. I thought I might be able to find something here to back-up what I'd already found. I think I'm just getting beat-up now & am no longer part of the conversation. There's no new information to be had here.
Thanks for the input.
RE: NPSH Margin in Vertical Turbine Pumps
One percent margin is acceptable unless the bid specifications say otherwise.
RE: NPSH Margin in Vertical Turbine Pumps
http://virtualpipeline.spaces.msn.com
"We can't solve problems by using the same kind of thinking we used when we created them." -Albert Einstein
RE: NPSH Margin in Vertical Turbine Pumps