Air in CH system and hot water returning to FE tank via the cold feed

[Tiggy1955]

I have a problem with air being sucked into my CH system creating airlocks in the radiators. The water is flowing back into the FE tank via the cold feed pipe. I can feel warm water coming through the feed pipe back into the tank as the tank water level slowly get higher. I can hear the overflow gurgling in the FE tank.

The system is 20 years old but the Worcester Bosch boiler is only 9 years old. All has worked perfectly well. I did have the classic blockage where the cold feed meets the hot return but the clogged pipes have been cut out and replaced.

I have fitted a new pump and it is set to the lowest speed. All of the radiators have been bled many times and balanced.

So the heating is working fine except that I have this problem of the air displacing the water back to the FE tank. The water it getting back into the tank a quite a rate - I would say about 2 litres per hour. This means that the rads need to be bled constantly.

Any ideas? Could it be an problem with the boiler itself?

 

[Ric2013]

I think getting someone in may be a good idea. No point fitting a new boiler as a soution until you can be sure what the problem is. Good luck, and please do let us know how you get on - makes it worth our while, you know.

 

[Tiggy1955]

OK guys here is an update on my situation...............

Action taken yesterday:

• I fully drained the system.
• I fitted a brand new diverter mid-position valve. I did this because a) it was old, b) the CH and HW were not working together c) the system was empty so do it now as a preventative measure.
• I have filled the system with Sentinel X400 and that is currently still in the system.

Outcome:

• The system is working very very well - getting a lot hotter that it used to.
• The CH and HW work together now.
• The whole system seems quieter and more efficient.

But:

• The rads still need bleeding within 30 minutes of the CH starting up. One in particular is gurgling and this is the one loosing most of it’s water back to the FE tank.
• The FE tank is still getting water pushed back into it via the flow outlet at the bottom of the tank. I know this because, apart from the rads getting cold at the top, if you watch it for 5 minutes you can actually see the levels rising and you can see murky water entering via the flow outlet. The tank water was perfectly clear yesterday, now it’s rusty red (well at least I guess the X400 is doing it’s job .
• When I bleed the rads the water level in the FE drops back to the correct level.

Planned next steps:

• Leave the X400 in for a couple more days and see if this makes any difference.
• Drain, flush and add some X100 inhibitor.
• Test for another couple of days.
• If I still have the back fill/bleeding problem call a good Heating Engineer for advice.
• Go off and resolve the Brexit Crisis because that looks a lot easier

Thank you all for your help - I’ll keep you posted.

 

[John.g]

OK guys here is an update on my situation....

Action taken yesterday:

• I fully drained the system.
• I fitted a brand new diverter mid-position valve. I did this because a) it was old, b) the CH and HW were not working together c) the system was empty so do it now as a preventative measure.
• I have filled the system with Sentinel X400 and that is currently still in the system.

Outcome:

• The system is working very very well - getting a lot hotter that it used to.
• The CH and HW work together now.
• The whole system seems quieter and more efficient.

But:

• The rads still need bleeding within 30 minutes of the CH starting up. One in particular is gurgling and this is the one loosing most of it’s water back to the FE tank.
• The FE tank is still getting water pushed back into it via the flow outlet at the bottom of the tank. I know this because, apart from the rads getting cold at the top, if you watch it for 5 minutes you can actually see the levels rising and you can see murky water entering via the flow outlet. The tank water was perfectly clear yesterday, now it’s rusty red (well at least I guess the X400 is doing it’s job .
• When I bleed the rads the water level in the FE drops back to the correct level.

Planned next steps:

• Leave the X400 in for a couple more days and see if this makes any difference.
• Drain, flush and add some X100 inhibitor.
• Test for another couple of days.
• If I still have the back fill/bleeding problem call a good Heating Engineer for advice.
• Go off and resolve the Brexit Crisis because that looks a lot easier

Thank you all for your help - I’ll keep you posted.

Thanks for the feed back, did you try the pump on PP control?.

 

[Tiggy1955]

Thanks for the feed back, did you try the pump on PP control?.

Going to do that today. Will let you know - thanks.

 

[Tiggy1955]

Thanks for the feed back, did you try the pump on PP control?.

John G you are a star!!! Set the pump to PP2 and all is sweet! I thank you sir.

Would you mind spending 2 mins explaining to me in laymans terms exactly what the Proportional Pressure setting does? It must be more that just a lower pressure setting - thanks.

 

[doitmyself]

Yes the tank is full. As the heating runs I can see the sediment being moved around the FE tank. I put my hand in the tank and you can feel warn water coming back in via the feed outlet.

I see that you have 'solved' the problem by setting the pump to PP2. However this may be a compromise.

When the water is heated it will expand so the water level in the FE tank will rise and feel warm (hot water rises).

The level should be adjusted, by bending the ballcock valve stem, so the tank is only half full when the water is hot.

If the level is too high water will escape via the overflow pipe. So when it cools down the level in the tank drops and has to be replenished via the ballcock valve. This introduces more air to the system meaning more bleeding.

 

[John.g]

John G you are a star!!! Set the pump to PP2 and all is sweet! I thank you sir.

Would you mind spending 2 mins explaining to me in laymans terms exactly what the Proportional Pressure setting does? It must be more that just a lower pressure setting - thanks.

Good to hear that the pump over has stopped, I assume that you checked it with CH only & HW only. One concern I have is that you may have a partial blockage of the boiler heat exchanger as you ran for years with no pump over on a fixed speed setting, if there is a blockage and it gets progressively worse the the pump on PP control will just keep modulating down and the boiler deltaT will keep increasing for any given firing rate, I think some boilers cut out if the deltaT exceeds 25C or 30C, on the other hand you may have no blockage and/or you may have cleared it out with the chemical addition. Pump PP control is not recommended for boilers with a ABV (auto bypass valve) which opens on circ pump over run (if installed) for a short time on boiler shutdown to remove the residual heat from the exchanger, this is no problem with a fixed speed pump as the pump head will rise to its max (4M in your case) when all the zone valves shut so th ABV can be set at say ~ 3M so that it will open only on boiler shutdown, On PP control, the pump will reduce its speed to maintain its minimum head of ~ 1.2M but if you set the ABV down to say 0.8M then when the boiler comes back on the pump will ramp up to maybe 2M or so and there will be excessive bypass at this pressure. Again your boiler may not be fitted with this or it may use the post air purge to cool down the exchanger.
Now for the good news....pump PP control.
PP control was introduced on A rated circ pumps to save energy and in some cases to reduce noisy TRV,s when throttling down.
I have one myself (Wilo) which consumes 21/23 watts with everything opened up and falls to 12/14 watts on CH only when some of the TRVs are throttled down.
They work like this, depending on the PP setting you select the pump then sets a minimum head at zero flow and a maximum head at its full flow. For example assume that PP3 setting is selected on the UPS2, at that setting (see page 11 of the manual), the pump will modulate between 0 flow at 1.2M & 2.15M3/h (36 LPM) at a 3M head.
Now assume that the pump is running on fixed speed1 and the system with everything opened up requires a 2.9M head at a f/rate of 0.9 M3/h (15 LPM).....you now change over to PP3 control, the pump will go minimum speed and then starts ramping up, for any given point on that "curve" the pump calculates the exact power needed and compares this with the actual absorbed pump power and because there is only one point on this (or any) curve where that calculated power and the absorbed power are exactly equal then the pump will stop ramping and remain at this setting until the system conditions change. I am able to calculate this in a spreadsheet (unfortunately that I am unable to post on here) so if we go back to our original requirement of a 2.9M head at 15 LPM and c/o to PP control then the pump head and f/rate will fall to 1.8M head & 11.6 LPM, as the system requirements fall then the pump will modulate still further. Again if you are back to fixed speed and you shut off "1/2" the rads you might need a 2M head for a f/rate of 7.5 LPM, change back to PP control and the head will fall to 1.52M & the f/rate to 6.7 LPM. If you "dead headed" the pump by say shutting the pump discharge isolating valve, the pump head will fall to 1.2 M at zero F/rate, if you fitted a controllable by pass around the pump and started opening it, the pump would ramp up to a 3 M head & a f/rate of 2.15 M3/h or 36 LPM.

Edit: Should have asked, what PP setting are you using??, thanks.
Have just seen that you are on PP2, I will adjust the numbers above shortly to reflect this, I would suggest PP3 if still no pump over.
I have left the above PP3 and shown the PP2 settings below, very little difference, one of the draw backs of UPS2 PP control.

PP2 SETTING
assume that the pump is running on fixed speed1 and the system with everything opened up requires a 2.9M head at a f/rate of 0.9 M3/h (15 LPM).....you now change over to PP2 control, the pump will go minimum speed and then starts ramping up, for any given point on that "curve" the pump calculates the exact power needed and compares this with the actual absorbed pump power and because there is only one point on this (or any) curve where that calculated power and the absorbed power are exactly equal then the pump will stop ramping and remain at this setting until the system conditions change. I am able to calculate this in a spreadsheet (unfortunately that I am unable to post on here) so if we go back to our original requirement of a 2.9M head at 15 LPM and c/o to PP2 control then the pump head and f/rate will fall to 1.58M head & 11.1 LPM, as the system requirements fall then the pump will modulate still further. Again if you are back to fixed speed and you shut off "1/2" the rads you might need a 2M head for a f/rate of 7.5 LPM, change back to PP2 control and the head will fall to 1.35 M & the f/rate to 6.2 LPM. If you "dead headed" the pump by say shutting the pump discharge isolating valve, the pump head will fall to 1.1 M at zero F/rate, if you fitted a controllable by pass around the pump and started opening it, the pump would ramp up to a 2.7 M head & a f/rate of 2.34 M3/h or 39 LPM.

 

[doitmyself]

I am able to calculate this in a spreadsheet (unfortunately that I am unable to post on here)

You can post it if you zip it first. I would be interested in seeing the spreadsheet.

 

[Ric2013]

Just in case you didn't follow that, and I'm not sure I did, here is another very rough explanation of PP as explained to me by a Grundfos engineer.

Very basically, a pump could run faster and slower to maintain the same available head as rad valves are open and shut. When a valve is opened, more water can flow so the pump runs faster to maintain the same pressure. This would be a constant pressure setting.

Proportional pressure slightly over-compensates, so as the flow increases when you (or a TRV) open the flow to a rad, the pressure at the pump is not only maintained by increasing the pump rotation speed, but the pressure is actually raised a little. The reason for this is that the primary circuit (the pipe from the boiler to the motorised valve and the common return to the boiler) creates more drag when the water velocity is higher. So if the pump merely maintained a constant pressure at the pump, the pressure at each radiator would drop when all valves were open and each radiator would still receive a little less water than if only half were turned on. By over-compensating, the pump makes up for the increased drag on the primary circuit as velocity increases.

On the UPS2 (and I would imagine most pumps are similar), the PP1,2, and 3, differ in that the PP3 does the most overcompensation, and the PP1 does the least.

 

[John.g]

You can post it if you zip it first. I would be interested in seeing the spreadsheet.

There you go, works exactly as the spreadsheet shows.

 

[John.g]

Just in case you didn't follow that, and I'm not sure I did, here is another very rough explanation of PP as explained to me by a Grundfos engineer.

Very basically, a pump could run faster and slower to maintain the same available head as rad valves are open and shut. When a valve is opened, more water can flow so the pump runs faster to maintain the same pressure. This would be a constant pressure setting.

Proportional pressure slightly over-compensates, so as the flow increases when you (or a TRV) open the flow to a rad, the pressure at the pump is not only maintained by increasing the pump rotation speed, but the pressure is actually raised a little. The reason for this is that the primary circuit (the pipe from the boiler to the motorised valve and the common return to the boiler) creates more drag when the water velocity is higher. So if the pump merely maintained a constant pressure at the pump, the pressure at each radiator would drop when all valves were open and each radiator would still receive a little less water than if only half were turned on. By over-compensating, the pump makes up for the increased drag on the primary circuit as velocity increases.

On the UPS2 (and I would imagine most pumps are similar), the PP1,2, and 3, differ in that the PP3 does the most overcompensation, and the PP1 does the least.

Just in case you didn't follow that, and I'm not sure I did, here is another very rough explanation of PP as explained to me by a Grundfos engineer.

Very basically, a pump could run faster and slower to maintain the same available head as rad valves are open and shut. When a valve is opened, more water can flow so the pump runs faster to maintain the same pressure. This would be a constant pressure setting.

Proportional pressure slightly over-compensates, so as the flow increases when you (or a TRV) open the flow to a rad, the pressure at the pump is not only maintained by increasing the pump rotation speed, but the pressure is actually raised a little. The reason for this is that the primary circuit (the pipe from the boiler to the motorised valve and the common return to the boiler) creates more drag when the water velocity is higher. So if the pump merely maintained a constant pressure at the pump, the pressure at each radiator would drop when all valves were open and each radiator would still receive a little less water than if only half were turned on. By over-compensating, the pump makes up for the increased drag on the primary circuit as velocity increases.

On the UPS2 (and I would imagine most pumps are similar), the PP1,2, and 3, differ in that the PP3 does the most overcompensation, and the PP1 does the least.

I would like to ask that grundfos engineer why in a 6M pump that they only allow a max 3M PP head, even the "cheap" pumps allow a 5 M PP head. I think that even the UPS3 only has a max PP setting of 3.5M.
If you take the above example that I used and assume a perfectly normal CH system. Ideally to set up the PP control, one should open up all the zone valves including HW and open all or any TRVs fully to get the maximum flow, you can then calculate the head and flow rate, I did mine by measuring the boiler deltaT and because I knew its output I was able to calculate the flow rate, I then looked at the (fixed) speed pump curve and was able to read off the head.
So if the head & flow required are 2.9M @ 15 LPM, you should then be able to set the PP control high enough to give you this but because the UPS2 can only be set to a max of 3M the head and flow will fall to 1.8M & 11.6 LPM so you are getting 77% of the max flow. IF you could increase that PP setting to 4M (3.8M to be exact) then you would have the required head & flow of 2.9M & 15 LPM on change over to PP mode. I know this is exactly how it works because I can set my Wilo pump any where between 0.5 M & 5.5 M PP head in increments of 0.1 M so if I set it to the 3.8 M above I will get that 2.9M head & 15 LPM, it will never go any higher but will ramp down as I described on reducing heat demand.

 

[John.g]

You can post it if you zip it first. I would be interested in seeing the spreadsheet.

Here is very interesting article on Grundfos AuotAdapt.

 

[Tiggy1955]

I would like to ask that grundfos engineer why in a 6M pump that they only allow a max 3M PP head, even the "cheap" pumps allow a 5 M PP head. I think that even the UPS3 only has a max PP setting of 3.5M.
If you take the above example that I used and assume a perfectly normal CH system. Ideally to set up the PP control, one should open up all the zone valves including HW and open all or any TRVs fully to get the maximum flow, you can then calculate the head and flow rate, I did mine by measuring the boiler deltaT and because I knew its output I was able to calculate the flow rate, I then looked at the (fixed) speed pump curve and was able to read off the head.
So if the head & flow required are 2.9M @ 15 LPM, you should then be able to set the PP control high enough to give you this but because the UPS2 can only be set to a max of 3M the head and flow will fall to 1.8M & 11.6 LPM so you are getting 77% of the max flow. IF you could increase that PP setting to 4M (3.8M to be exact) then you would have the required head & flow of 2.9M & 15 LPM on change over to PP mode. I know this is exactly how it works because I can set my Wilo pump any where between 0.5 M & 5.5 M PP head in increments of 0.1 M so if I set it to the 3.8 M above I will get that 2.9M head & 15 LPM, it will never go any higher but will ramp down as I described on reducing heat demand.

So in really simple non-technical terms:

A pump set to a Fixed Speed will apply a constant speed/pressure regardless of what’s ahead of it in the system. The result being that it could be too much pressure (particularly when a change takes place such as some rads being closed off) and it is also inefficient.

A pump set with Proportional Pressure will apply a variable speed/pressure depending on what is ahead of it (when a rad is closed/opened the pump compensates accordingly). The result being a more appropriate pressure is applied and it is more efficient.

Is that about right?

 

[Tiggy1955]

I have one final question on this topic:

I replaced the old Grundfoss UPS pump (because it was old) with the Grundnfos UPS2. I got the UPS2 because that seemed to be the direct replacement for the UPS.

Until John G mentioned PP I had never heard of it. What’s more, I did not even know that the UPS2 had PP.


My question is: If I had not replaced the pump I would have been left with a pump that only had Fixed Speeds. In which case, how could I have resolved the pump over problem if the slowest speed of the pump was still too much?

 

[John.g]

I have one final question on this topic:

I replaced the old Grundfoss UPS pump (because it was old) with the Grundnfos UPS2. I got the UPS2 because that seemed to be the direct replacement for the UPS.

Until John G mentioned PP I had never heard of it. What’s more, I did not even know that the UPS2 had PP.


My question is: If I had not replaced the pump I would have been left with a pump that only had Fixed Speeds. In which case, how could I have resolved the pump over problem if the slowest speed of the pump was still too much?

With your system like Ric2013 has shown above, cold feed before the boiler and vent after it I am a bit surprised that you wern't get some pump over "all the tine" depending on the number of rads in service. The cure: ideally I would ensure that the boiler heat exchanger has no (or partial) blockage but of course you need a RGI to do this. If you are happy not to inspect it then if you want to retain the gravity system you could shift the cold feed from before the boiler to after it adjacent to the vent but not more than 150mm away from it OR fit a fully pressurized system with a expansion vessel.

If the PP control is "curing" the problem then why worry too much?.

Are all your rads etc heating up to your satisfaction?.

I don't know if you have a boiler flow temperature indication but (if so) sometime you might watch it when the boiler shuts down and see what the temperature rise is over the next few minutes.
All this has been and is very very interesting, thanks for the feed back.

 

[Chuck]

So in really simple non-technical terms:

In an ideal world, the pressure drop across a given radiator would always be the same. The flow through this radiator is then limited by the lockshield valve and controlled by the local TRV.

A so-called 'constant pressure' pump, which adjusts its displacement rate to achieve a fixed pressure difference across its ports, will give a constant pressure drop across the radiators provided there is no pressure drop along the connecting pipework.

In practice, there will will be a flow-dependent pressure drop due to the connecting pipework. The 'proportional pressure' behaviour of a smart pump is an attempt to cancel this out.

Constant pressure operation is definitely, in my opinion, an improvement over a traditional constant speed pump, although it makes setting up the external by-pass correctly a rather delicate operation. Whether the additional complication introduced by PP is actually worthwhile in practice I'm not so sure about; the theory is based on an assumption about the pipework that is at best a rough approximation.

 

[Tiggy1955]

With your system like Ric2013 has shown above, cold feed before the boiler and vent after it I am a bit surprised that you wern't get some pump over "all the tine" depending on the number of rads in service. The cure: ideally I would ensure that the boiler heat exchanger has no (or partial) blockage but of course you need a RGI to do this. If you are happy not to inspect it then if you want to retain the gravity system you could shift the cold feed from before the boiler to after it adjacent to the vent but not more than 150mm away from it OR fit a fully pressurized system with a expansion vessel.

If the PP control is "curing" the problem then why worry too much?.

Are all your rads etc heating up to your satisfaction?.

I don't know if you have a boiler flow temperature indication but (if so) sometime you might watch it when the boiler shuts down and see what the temperature rise is over the next few minutes.
All this has been and is very very interesting, thanks for the feed back.

I'm draining the system down right now to remove the X400 and flushing through. I will refill and add the X100. All rads working really well (better that they have for a long time) and HW piping hot so I'm going to stick with the PP control.

 

[John.g]

So in really simple non-technical terms:

A pump set to a Fixed Speed will apply a constant speed/pressure regardless of what’s ahead of it in the system. The result being that it could be too much pressure (particularly when a change takes place such as some rads being closed off) and it is also inefficient.

A pump set with Proportional Pressure will apply a variable speed/pressure depending on what is ahead of it (when a rad is closed/opened the pump compensates accordingly). The result being a more appropriate pressure is applied and it is more efficient.

Is that about right?

More or less, a fixed speed pump head falls as the flow rate increases and increases with flow rate decrease (Trv's or zone valves closing) where as PP control works in the opposite sense, as the flow rate increases the pump head increases (pump ramps up the speed) and visa versa. Most of these pumps also have CP (constant pressure) control where the head is kept constant whatever the flow rate is.

 

[John.g]

In an ideal world, the pressure drop across a given radiator would always be the same. The flow through this radiator is then limited by the lockshield valve and controlled by the local TRV.

A so-called 'constant pressure' pump, which adjusts its displacement rate to achieve a fixed pressure difference across its ports, will give a constant pressure drop across the radiators provided there is no pressure drop along the connecting pipework.

In practice, there will will be a flow-dependent pressure drop due to the connecting pipework. The 'proportional pressure' behaviour of a smart pump is an attempt to cancel this out.

Constant pressure operation is definitely, in my opinion, an improvement over a traditional constant speed pump, although it makes setting up the external by-pass correctly a rather delicate operation. Whether the additional complication introduced by PP is actually worthwhile in practice I'm not so sure about; the theory is based on an assumption about the pipework that is at best a rough approximation.

I picked up this description of PP control somewhere along the line and it bears out what you are saying.
I would have to say that PP control works very well for me.

PP Control
"It starts with the assumption that about half of your pressure loss in the system will be in the distribution pipe while the other half is lost in the radiators. Consequently, the pump is controlled such that it will respond to a decrease in flow with a reduction of its head and that at zero flow, when all valves are closed, it will provide half the head pressure it has at maximum flow."

 

[doitmyself]

There you go, works exactly as the spreadsheet shows.

Unfortunately the spreadsheet is difficult to understand as you don't explain where the data comes from or what each column contains.

For example:
How did you obtain the Know Head and Known Flow?
Where does the UPS2 data at the top come from? It doesn't agree with the Grundfos published data.
What does "rem 7.9 lpm" mean (apart from the obvious litres per min)?
What does series 1 and series 2 refer to?
etc etc.

 

[doitmyself]

Here is very interesting article on Grundfos AuotAdapt.

The file will not open.

 

[John.g]

I have one final question on this topic:

I replaced the old Grundfoss UPS pump (because it was old) with the Grundnfos UPS2. I got the UPS2 because that seemed to be the direct replacement for the UPS.

Until John G mentioned PP I had never heard of it. What’s more, I did not even know that the UPS2 had PP.


My question is: If I had not replaced the pump I would have been left with a pump that only had Fixed Speeds. In which case, how could I have resolved the pump over problem if the slowest speed of the pump was still too much?

The file will not open.

Try this link so.
The Grundfos AUTOADAPT algorithm

 

[John.g]

Unfortunately the spreadsheet is difficult to understand as you don't explain where the data comes from or what each column contains.

For example:
How did you obtain the Know Head and Known Flow?
Where does the UPS2 data at the top come from? It doesn't agree with the Grundfos published data.
What does "rem 7.9 lpm" mean (apart from the obvious litres per min)?
What does series 1 and series 2 refer to?
etc etc.

I would have to spend a very long time explaining the whole spreadsheet data etc but if you click in any of the cells (assuming you are familiar with s.heets) you can see every calculation carried out, however I will try and answer some/most of your queries.
The known head and known flow are from my own system, I derived it years ago by measuring the oil fired boiler deltaT, then knowing the boiler output I was able to calculate the flow rate, I then went to my pump (a salmson at that time) and just read off the fixed speed pump head at that flow. Every installation is different of course but even if you have no idea what it is, if you select PP3 on the UPS2 you may find that it will be perfectly adequate, I use a different pump (Wilo) which gives far more options and I run it at a PP head of 4M to give me what I want.

"UPS data on the top??" it comes from the PP curves in page 11 of the attached UPS2 file and I would venture that it is reasonably accurate given that I am reading it off a plain sheet.

"rem 7.9 LPM" was just some reminder to myself when building the spreadsheet.

series1 & series2 are just excel assigned labels for the two trend lines, just place the cursor above the labels and the data columns will be highlighted, the x axis (horizontal) is the pump head in meters and the Y axis (vertical) is the pump flow in LPM.
The point where the two trend lines intersect is (or should be) the actual head and flow rate achieved with a UPS2 pump on PP setting 3 based on my known values.

Should also have said that if you place the cursor in either of the trend lines and click on it that it will highlight the data for that particular trend line, if you place it in the trend line without clicking it will give you the two values at that particular point.

 

[doitmyself]

I would like to ask that grundfos engineer why in a 6M pump that they only allow a max 3M PP head

The simple answer is efficiency. The pump efficiency peaks around the middle of the curve.

 

[doitmyself]

The known head and known flow are from my own system, I derived it years ago by measuring the oil fired boiler deltaT, then knowing the boiler output I was able to calculate the flow rate, I then went to my pump (a salmson at that time) and just read off the fixed speed pump head at that flow.

That just gives you the working point when that particular pump is used. That may not be the same as the required working point.

Here's a example, using my system which has a UPS2:

The required flow rate and head are 8 litres/min at 2.2m. The actual working point, shown by the yellow dot, is 9.99 lpm at 3.43m which is where the pump curve and system curve (red line) meet. See graph below.

If a PP setting is used, it needs to provide the required flow/head not those obtained by the fixed speed setting.

The attached UPS2 file is corrupted