Pump Efficiency, Head, Flow, and related technical info

[chem geek]

I'm adding this thread in The China Shop to move the more technical discussion that was originally started in this thread (http://www.poolforum.com/pf2/showthread.php?t=6403) at post #14 and should get moved into this thread so that we can continue the discussion without scaring off newbies. Any net results or simple rules can be posted back into the original thread, but here in this thread we are free to use the mathematics of fluid dynamics and statics.

[chem geek]

Mark,

I also made a spreadsheet which is how I came up with the formula, and I carefully measured the graphs with a ruler to get reasonable accurate numbers. My data, from both the full IntelliFlow and the IntelliFlow 4x160 graphs, is as follows:
(I'm continuing to edit this to straighten out the columns)


GPM Head Out. Power In. Power Eff. (RPM/350)^2-(GPM^2)/470
(ft.) (RPM/322)^3+80
3450 RPM
0 96 0 1310 0.0% 97.180164 1310.277154
20 94 353.7502 1620 21.8% 96.32910017
40 93 699.9738 1930 36.3% 93.77590868
60 89 1004.8011 2210 45.5% 89.52058953
80 84 1264.4688 2510 50.4% 83.56314272
100 77 1448.8705 2780 52.1% 75.90356826
120 67 1512.8466 2980 50.8% 66.54186613
140 56 1475.2136 3010 49.0% 55.47803634

3110 RPM
0 80 0 78.95591837 980.9766836
20 79 297.3007 78.10485454
40 76 572.0216 75.55166305
60 71 801.5829 71.2963439
80 65 978.458 65.33889709
100 57 1072.5405 57.67932262
120 48 1083.8304 48.3176205

2350 RPM
0 46 0 45.08163265 468.7191816
20 45 169.3485 44.23056882
40 42 316.1172 41.67737733
60 38 429.0162 37.42205818
80 31 466.6492 31.46461138

2070 RPM
0 35 0 330 0.0% 34.97877551 345.6705539
20 34 127.9522 450 28.4% 34.12771168
40 32 240.8512 550 43.8% 31.57452019
60 28 316.1172 630 50.2% 27.31920104
80 22 331.1704 690 48.0% 21.36175423

1500 RPM
0 19 0 18.36734694 181.0895264
20 18 67.7394 17.51628311
40 15 112.899 14.96309162
60 11 124.1889 10.70777247

950 RPM chart said 750, but was probably wrong
0 7 0 7.367346939 105.6804838
20 6 22.5798 6.516283109

690 RPM
0 4 0 95 0.0% 3.886530612 89.83965015
20 3 11.2899 95 11.9% 3.035466782

I do not get the same data you do in your table for actual GPM. For example, at 3450 RPM and a head of 80 feet, the graph looks like this is 90 GPM, not the 97 "Actual GPM" shown in your table. I understand the pump affinity equations that are valid in regions of equivalent efficiency. I just was curiously looking for a general solution. I believe what I said before to be true, that the formula I came up with is within 1-2 feet of head in accuracy which probably means that it is accurately reflecting what is going on -- a static head based on RPM^2 minus a dynamic head based on GPM^2. The "static head" is really a balanced dynamic head between the motor pushing water one way and it leaking at the same rate the other way. The GPM^2 term appears to just be the dynamic head of the net amount of flow through the pump so while the RPM^2 "push" amount remains constant (since we are looking at a curve at constant RPM), the "leakage" amount decreases as the head decreases so that a net GPM increases. Or another way of looking at it is that the pump RPM is pushing water at a GPM determined from (RPM/350)^2-(GPM^2)/470 = 0; GPM = sqrt(470*(RPM/350)^2) = RPM/16.1 so at 3450 this is 214 GPM. So the pump's RPM (and impeller size) cause 214 GPM to move when there is no head. Any resistance (head) results in a backward "leakage" which causes the net GPM to drop (since this backward movement meets a lot of frictional resistance), but 214 GPM is always being moved "forward" by the pump even when the net GPM is 0 (meaning that the "leakage" is also 214 GPM so no net movement is seen). At least this is my best understanding of how this works. I don't have the pump curves (for this pump) going down towards 0 head, but I have seen other pumps' curves that do appear to have the parabolic shape (see this link (http://www.manatron.net/Pdf's/JANDY%20MANUALS/mhp.pdf), for example).

Regardless of which formula is used, I also wanted to estimate the electrical efficiency and that has been harder to determine. Unfortunately, only 3 RPMs showed electrical power curves on the graph so my best-guess formula isn't validated very well, but it does appear to roughly be a combination of some small fixed losses (resistance, probably) plus an amount of "work" that is related to the cube of the RPM. This makes sense since the velocity of water is proportional to the RPM as is the GPM (as shown with the formula in the previous paragraph) while the frictional losses (i.e. head) are roughly proportional to the GPM^2 so the power is expected to be the product of the flow rate times head so proportional to GPM^3 and since GPM and RPM are directly related, this is proportional to RPM^3. What is harder to figure out is how the electrical power doesn't track the output power or the amount of head as might be expected. It instead seems to have a linear increase with net GPM and then slows down its increase as it approaches around 50% efficiency. I would presume that eventually as output power dropped at lower GPM, that the electrical power would start to drop as well. The electrical power should be directly related to the pressure resistence against the impellers (I'm assuming a constant RPM) which is a difference in pressure on one side of the impeller compared to the opposite side. So normally one would expect the electrical power to be proportional to head alone, but apparently the "leakage" causes some of the pressure on the opposite side of the impeller to be higher so that the net difference isn't the full amount of head (so there is less net pressure and therefore less "work"). As the head declines, the leakage also declines and apparently reduces the pressure on the opposite side of the head faster than the overall head drop so that there is a net electrical power increase. Near the point of optimal efficiency, these two effects act so that the amount of electrical power tracks the output power (near 50% efficiency) which essentially means that the "leakage" reduces the back pressure faster than the drop in overall head, but at a rate that is similar to the output power. I suspect that in the region at lower head and high GPM that the electrical power drops in rough proportion to the head since the "leakage" effect would be much smaller at that point. So, at very low head, the pump curve should be near vertical instead of the parabolic formula that I came up with (assuming that the leakage becomes minimal at low head). It seems like I'm missing something here, at least for figuring electrical power -- either that or it truly is as complicated as it sounds and not easily computed.

Richard

[mas985]

It was probably a good idea to move this thread into the china shop. It was starting to get a bit heavy for the construction forum. Not too many people want to get into the details of hydraulics so I usually give simple approximate answers. But I tend to get a better understanding of rules of thumb by getting into the details. On to the discussion at hand………


Curve Fitting

Taking data off of a picture is bound to generate significant errors depending on who does it and how. However, I went back and looked at the chart again, I enlarged the head graph, placed grids over it and I got closer to 95 GPM so I think we are both reading it differently. Anyway, I have found that printed graphs tend to be somewhat inaccurate as well as difficult to read and I bet if you got the data directly from Pentair in tabular form, you might find it different than what is on the graph.

Static Head

Next, I wanted to more clearly define static head so there is no confusion. The classical definition of static head loss in hydraulics is vertical lift or how far the pump must lift the water in a pipe to a different elevation. This type of head loss is independent of flow rate, depends only on vertical distance traveled and is not related to pumps at all. Dynamic head loss is the opposite where it depends on the velocity of water and the pipe/fitting it is going through.

Also, the pump itself will not have any signicant amount static head loss so to describe the head equation as having a static part and a dynamic part is probably not valid. As far as the pump head curve is concerned, a pump does not care if it is subjected to static or dynamic head, head loss is head loss which is resistance to flow. However, a pump responds to different head loss with varying flow rates which is were the head curve comes from. The way I like to think of it is that the pump causes flow, the flow causes head loss in the plumbing, the head loss causes the flow to slow down in the pump and so on. It is circular but can be solved in closed form or by iteration depending on the head loss curve formula.

Pump Conservation of Energy

As for pumping theory, total energy within the pump system must be conserved where water flow is only one part of the total energy. So even if GPM decreases, it does not mean the total energy does or that it is somehow lost to “leakage”. The motor delivers energy to the shaft as BHP and the impeller then transfers that energy as both pressure and flow. So full energy transfer equations of a pump are:

Motor Formula:
Kwatts (Energy Usage) / .746 = IHP (Input Horsepower)
IHP * Motor Efficiency = BHP (Braking Horsepower)

Pump Formula (exclusive of motor)
BHP * Pumping Efficiency = WHP (Water Horsepower)

Water Horse Power Conversion Formula
WHP * 3960 = Head * GPM

So the total efficiency of a pump is
Total Pump Efficiency = Motor Efficiency * Pumping Efficiency

So as head increases and GPM decrease, WHP would be constant if the pumping efficiency stayed constant. This is the reason I started with this equation to model the head curve. However, pumping efficiency is not constant and is dependent on both flow and head, and it usually peaks near the mid point of the head curve. So GPM is not really “lost” at high head due to "leakage" but it's energy is transfered to pressure or high head such that energy is conserved via Head * GPM. So another way to think about it is those "extra" GPMs are staying in the pump housing and creating more pressure rather than leaving the pump to create flow.

Motor efficiency losses are due to the I^2R losses in the windings, electromagnetic radiation, and friction in the motor. Pumping efficiency losses are due to the friction losses in the pump housing and head losses near the impeller and before exiting the pump housing.

As you have found, motor efficiency is much more difficult to model than pumping efficiency. Few manufactures, if any, will show energy consumption as a function of motor load. As a general rule of thumb, there is a sweet spot for pumps where the pumping efficiency reaches a maximum for a particular head value and the motor efficiency also reaches a maximum for a particular head value which is usually between (75% -100% of load). Too little or too much load and the motor efficiency goes down. A well designed pump will optimize both and together they will give an optimum efficiency over a range of head values.

Just getting data on electric motor energy efficiency is difficult at best. It is usually not published or only noted as peak efficiency. A call to the manufacture may get you the data but I have not been successful to date.

Although it is a noble effort to try and model the pump with great precision, given the uncertainties involved and lack of data, I think a rough approximation of energy savings should be sufficient for economic business case to see if it is worth it. With variable speed pumps, you will get your best energy efficiency at the lowest RPM. However, you need sufficient flow to give you at most two turnovers a day which is only 22 GPM over 24 hours. Using the .03 * RPM formula gives close to 750 RPM for 22 GPM.

I am not sure what electric power curves you are referring to but if you have one for 750 RPM, then you can determine the energy usage in 24 hours and compare it to two turnovers of your existing pump and see the difference. From the data you gave previously, your old pump required 6 hours for 2 turnovers (solar off) @ 950 watts which would be 5.7 kwatts/day.

Here are a few more good papers/sites that I have found which goes over many of the details of pump and plumbing systems.

http://www.pumped101.com/efficiency.pdf
http://www.pacificliquid.com/pumpintro.pdf

[chem geek]

Mark,

I know I'm being a mensch about this, but are you looking at this PDF file (http://www.pentairpool.com/misc/owners_manuals/pumps/IntelliFlo_Install_User_Guide.pdf) on page 47 with the graph "IntelliFlo Flow and Power vs Flow Pump Curve" and then starting with 80 feet on the left and moving across that horizontal line until it intersects the black line "Head @ 3450 RPM"? It not only visually looks almost exactly halfway between the 80 and 100 vertical lines for GPM, but it measures that way also -- possibly at 91. I zoomed in a whole lot just to make sure. If I look at this PDF file (http://www.pentairpool.com/misc/owners_manuals/pumps/IntelliFlo_4X160_Guide.pdf) which is in the 4x160 manual on page 25, then I can get something more like 92 which is getting closer to your number. Note that there are 4 vertical lines between 80 and 100 so that is 5 sections so each vertical line represents 20/5 = 4 GPM and the intersection is at the 3rd vertical line (after the 80 vertical line) so that is 12 GPM more than 80 or 92 GPM. I suspect that you counted each vertical line as being 5 GPM instead of 4. I discovered this unusual vertical line spacing (i.e. 4 lines instead of 3) because I used a ruler to measure between the two marked vertical lines (80 and 100) and didn't worry about those intermediate lines.

If you look at the first of the two links above showing the full IntelliFlo manual, then that graph does show the power (electrical) consumption curves for three RPM settings. That's how I got that data for my table.

So I looked at the documents you linked to and they are absolutely fantastic. Thank you so very much! When I referred to "leakage" it's really just a recirculation that is occurring (at a net 0 GPM and maximum head). There is no output work being done. I now see that this isn't a chamber or piston kind of pump effect, but a centrifugal impeller and vane technique so if the centrifugal added velocity goes against a pressure that brings the velocity back to zero, then there will be no net flow (but because this isn't the BEP point, there will be recirculation flows and uneven pressures in between the vanes and this can damage the pump).

The first document link you gave contained a very useful formula that helps figure out equivalent power efficiencies and identification of the most efficient point at each RPM. That is the definition of specific speed:

Ns = n * sqrt(Q) / H^(3/4)
or Specific Speed = RPM * sqrt(GPM) / (Head in Feet)^(3/4)

If I add this as a column to my spreadsheet, I find that though the specific speed varies with GPM and Head, the peak (electrical input to pump output) efficiency point at each RPM corresponds to roughly the same specific speed of around 1320. So that gives me additional useful information so that I will know if I am operating near the BEP point with both solar on and off (when I get my IntelliFlo pump).

I've made a detailed piping diagram for my system and the reason that my solar system has such high resistance is that it isn't on a single flat roof, but is on a roof with several hips so that the piping has a lot of 90 degree elbows and extra distance -- it's not at all a straight shot. There are 2 panels on one hip, 7 on another (5 higher and above 2 that are lower), 2 on another, and 1 on another. I did find a possible problem with the piping of the solar that could cause uneven flows (they didn't make the total path lengths the same throughout and instead did some Ts to return too soon so I essentially have two sets of solar panels with different path lengths). So my last 3 panels probably have lower flow than all the rest -- now I can understand why I actually saw a decrease instead of the expected increase in heat output when they added the most recent panel. They only worsened the already unbalanced situation. I'll calculate the expected flow rate difference and if it's significant, then I'll have them fix that as it should have been done correctly initially. Should be easy to fix by just breaking at the T and adding extra pipe.

Richard

[mas985]

I was using the brochure data but the manual is much better data and yes I get 92 GPM from that as well.

I can only find the energy usage curves for the Intelliflow. Are you assuming they are the same for the 4x160? I would check with Pentair on that to make sure they are the same.

Ok so with updated information, I plotted your plumbing curves (solar off/on) on top of the pump's head curve. Where they cross are your operatng points. I assumed your pump was at the same elevation as your pool.

http://i80.photobucket.com/albums/j188/mas985/Other/RichardsPool.jpg

You would get the same answer if you simultaneously solve your pump equation and your plumbing equation. So the crossover points follow the relationship of GPM = .0325 * RPM for solar off which is pretty close to what I had before. For solar on, the crossovers occur at GPM= .02 * RPM.

The only way to change your operating points is to change your plumbing. Otherwise the efficiency is what it is at those points. However, it does sound like you have an issue with your solar so if you are able to fix that it should move that curve to the right increasing the overall efficiency with solar on.

Good luck.

[mas985]

One more point that I think you touched on in your last post but I wanted to make sure it was not lost.

As you pointed out, energy use drops off as a cube of RPM so I think you will find that you will use the least amount of energy per GPM at the lowest RPM even if the efficiency drops somewhat with RPM. Assuming the maximum energy use is 3200 watts, here is my reasoning.

Watts / GPM = 3200 * (RPM/3450)^3 / GPM = 3200 * (RPM/3450)^3 / (.033 *RPM)

Watts / GPM = RPM^2 /405322.5

So the efficiency is not likely to roll off at a rate of RPM^2, so the lower the RPM the less energy is used.

Like I said before, if you operate at 750 RPM, you can do 2 turnovers in 24 hours and use the least amount of energy possible.

[chem geek]

Just FYI. I verified that the pump in the IntelliFlo and the IntelliFlo 4x160 are identical with identical curves and efficiencies. The only difference in the full version is the addition of a flow meter plus associated electronics to keep track of total volume so that the pump can shut off after a designated number of turnovers. That is what leads to much greater savings for certain configurations where multiple features are present (needing different flow rates) or where the system curve changes (e.g. filter gets dirty).

Richard

[waterbear]

Just FYI. I verified that the pump in the IntelliFlo and the IntelliFlo 4x160 are identical with identical curves and efficiencies. The only difference in the full version is the addition of a flow meter plus associated electronics to keep track of total volume so that the pump can shut off after a designated number of turnovers. That is what leads to much greater savings for certain configurations where multiple features are present (needing different flow rates) or where the system curve changes (e.g. filter gets dirty).

Richard
Actually, the actual pump itself is identical with the WhisperFlo. The only difference is the motor with all it's bells and whistles.

[msm859]

Can someone give me the short answer? Would it be more efficient(least costly to run) with the Intelliflo to have the slowest GPM to turn over 1x per day AND have the largest pipe with minimum 90's to have the lowest pressure/head???

I am having a pool built and using the Intelliflo and my builder thinks I am too concerned with the over use of 90's and pipe size. He indicates in the past--with the regular Whisperflo he has to use eyeballs to get the head up.

[mas985]

Low head loss in plumbing is a good thing up to a point. As head drops, flow rates increase but so does the power draw of the pump. The peak efficiency of a pump (GPM/Watt) is generally near the middle of the pump head curve.

Another consideration is if you have too little head on the return but too much head on the suction side, you run the risk of sucking in air or worse, pump cavitation.

The only down side of the opposite case (too much return head) is that it reduces the potential flow. So it is best to error on this side which is why most pool plumbing has larger suction pipes than return pipes.

So you really need to match your plumbing system with the pump. To do it properly requires a bit of work which is why most pool builders simply do what they have done before.

If you look at the curves (http://www.poolforum.com/pf2/showpost.php?p=41726&postcount=5) for Richard's pool and the Intelliflow, with the solar off is about as low a head I would go on that pump and with solar on is about as high as I would go so I think it would be well suited for his pool.

Usually 1 - 2 1/2" suction line and 1 - 2" return line is sufficient for most pools. If you have mutliple suction lines from pool to pad I would go with 2" lines and if you have more than 2 return lines, I would go with 1 1/2" return lines.

2 - 2" lines is about the same head loss as 1 - 2 1/2" line.
2 - 1 1/2" lines are about same head loss as 1 - 2" line.

Having said all that, it is much easier to add head to a plumbing system then it is to reduce it as your PB pointed out. So I would always error on the side of large pipes and use ball valves at the pad to control and balance the head for the suction and return. This way you can adjust the plumbing system to get the most GPMs/Watt no matter what pump is put on. Plus, it is difficult to predict exactly how much head a plumbing system will have and is best to measure it after the fact.

Also, post the details of your pool and equipement so we can comment further on the design.

BTW 2 x 45 degree bends are only slightly better than 1 x 90 degree.

[msm859]

Thanks for the explanation. It is an 18 x 36 pool with separate built in spa 6 jets, both have 400 sq" cartridge filters, 2 - intelliflo pumps, single 400 btu mastertemp heater, water feature with Pentair waterfall pump, still debating final finish.

[mas985]

You did not mention your plumbing. What does the pool builder want to put in and what do you want? Lines sizes, number lines, returns, skimmers, main drains, etc. Also, how far from pool to pad.

Your pool size is pretty close to mine and I have two skimmers, a split main drain and 4 returns.

Ideally, I would have each skimmer and the main drain pair on a separate 2" lines all the way back to the pad. 3, 2" lines are equilvalent to a single 3" line plus it will allow you to turn on just one of the three to isolate a suction line for repair or to drain the pool via the main drain only.

For the returns, you could go with one 2.5" line, two 2" lines or four 1.5" lines. Each configuration is equilvalent in terms of head loss. If the pad is close to the pool, you could go with 1, 2" or 2, 1.5" lines.

This should give you pretty close balance between suction and return. Adding ball valves at the pad to control flow will allow you to fine tune your flow rates.

[msm859]

I have two skimmers and the main drain with 3 - 2" lines going back to the pad which is @ 25' from the pool. There is a single 2.5" return line. Each line has a neverlube valve on it at the pad

There is no extra plumbing to divert the water to drain the pool via the main drain. Wouldn't there have to be a diversion valve to send the water somewhere other than back to the pool?

[mas985]

I have two skimmers and the main drain with 3 - 2" lines going back to the pad which is @ 25' from the pool. There is a single 2.5" return line. Each line has a neverlube valve on it at the pad

There is no extra plumbing to divert the water to drain the pool via the main drain. Wouldn't there have to be a diversion valve to send the water somewhere other than back to the pool?

Yes usually, a drain pipe is placed right after the pump with a manual valve so you can dump the water with either a hose or directly into a drain. You can also use flexible backwash hose to dump it on the lawn.

Also, it sounds like your plumbing is fine and will give you decent flow rates.