Insufficient flow in hydronic system
Last Post 19 Oct 2015 07:48 AM by chingo. 35 Replies.
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chingoUser is Offline
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09 Oct 2015 12:16 PM
I was wondering if anyone could answer a few questions. 1. which system would provide more flow using exact same equipment an open loop or a closed loop???? 2. If i have the exact same equipment but installed in 2 different locations (same length of pex etc...) should i not achieve similar flow???? 3. What would cause the pump to see a large amount of resistance in 1 system and not the other (given same equipment AND no air in system)???? 4. If system is running quiet and smooth and heated water is shown to be circulating via temp. gauges (SEND and RETURN) on manifold of zone then shouldn't the pump be considered to be good even though i am not getting calculated flow. OR might it still be defective.????? 5. Have you ever heard of getting 3 defective pumps in a system (system was put together by WATTS) Using purge cart hooked to system i can get a flow rate through system. 3GPM divide by 8 =.375gpm PURGE CART = 1hp submersible pump in 50 gallon tank and connected to system via 1/2" hose IN FLOW (at fill point) OUTFLOW (just before boiler) OPEN LOOP SYSTEM to and from 50 gallon opened air tank. any questions answered OR input would be appreciated. thanks neil
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09 Oct 2015 01:58 PM
1. Well they should be the same. In an open loop system, the heating branches off of and returns to the DWS(think offramp, loop and onramp)
2. Yes, assuming there are no differences in the installation
3. Something that is not similar(kinked crimped defective line, clogged manifold or valves ect)
4. How do you know it is not getting calculated flow?
5. Well parts sometimes are bad or arrive bad, but 3 in a row would be pretty rare IMO
That is a lot of HP for your test cart, are you using that to gauge your flow? The circ pump is surely a small fraction of that submersible and would deliver much lower fluid velocities turbulence and friction, so it is not really a valid way to compare flows.

What exactly is your problem? Not getting enough heat? Long runtimes to get to thermostat temp? Boler short cycling?

Got more system information? A system diagram would be great... Sounds like you have 8 loops, how long are the loops? What size pex? What are you using as a radiator? how many sq/ft? What are your calculated flows and temps. What are your actual temps? What size is your boiler.
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09 Oct 2015 02:11 PM
> OPEN LOOP SYSTEM to and from 50 gallon opened air tank

I would also consider circulation pump cavitation, ie, the static pressure at the pump intake. What does your pump require and can you get that in an open air system?
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09 Oct 2015 03:10 PM
 
To answer some questions on procedure.
I have the flow meters FULL OPEN
Adjustment to the run is done via the KEY NOT the Blue Adjustment Cap
ALL pumps are UPS 15-58 1 Main circulator 3 Zone Circulators.
There are 3 SS-Manifolds (see pic)
2 Are 8 Run ½” pex 250 feet +/-1%
1 Is 4 Run 1/2:” pex 250 feet +/-1%
ALL connections FEED and RETURN are ¾” pex from pump to manifold.
The zone that I have talked about previously is below the 3zone Watts distro unit.
It has approx. 10 feet of connecting pex FEED and RETURN.
The other two zones are 40 feet and 70 feet away from pump FEED and RETURN.
The MAIN LOOP (Boiler,exp tank etc….) see pics is joined with 1-1/4” copper
It is approx 16 feet loop length.
 
THIS SYSTEM HISTORY
 
PROJECT HOUSE/MAIN RESIDENCE
Designed to showcase all that I do.
 
This system was designed with country well water on property.
Rather than take a chance corroding system, I decided to use a closed loop.
I used and AXIOM MF200 System Feeder for my pressure/fill requirement on makeup.
 
When I first started system I used a purge cart
The main system was started up (call for pump start disabled) hose was connected to
Fill location and relief valve was left off (highest point of main loop.) hose attached and run back to purge cart. Ran system for 10 min. until filled and consistent flow.
NOTE: ALL Zone pumps were off.
Also water was prevented from entering or exiting zones. MAIN LOOP flow only.
Unhooked Purge cart and reattached relief valve and fill cap.
 
Started main system pump to circulate water. (MAIN LOOP only)
Zones are still isolated and pumps disabled.
AXIOM pres./fill is ON. Add water if needed. Pressure to 12psi.
Nice smooth operation (no crackle etc…)
Ran for 10 min. No Main flow meter to give reading. Assumed fine.
Pressure built to 12 psi, water was added (indicated by water line moving down in tank)
AXIOM turned off by itself and system continued to run with new settings for pres.
 
Turned off system and moved to manifold purge.
 
1hp pump in 53 gallons of clean water hooked to input of manifold on the FEED side.
On the RETURN side I attached a hose and ran it back to cart.
 
Pushed 2gpm through individual run on manifold and let run for 10 min.
Did each run on manifold individually. at same rate
 
Then ALL runs on flow meters read approx. 3/4gpm per run, STRONG AND STEADY
RAN for  10 min.
There should be no air left in the manifold system.
Turned off all Runs on manifolds at Feed and Return (Key and Meter)
Opened feed and return to MAIN LOOP.
Since I used shark bite fitting on OUT of pump and IN of Return manifold able to fill line by hand and reconnect.
 
System is now reconnected waiting to add zones to main loop.
I add the basement loop first. (8 run manifold located below main panels 200’ of ½” pex each run.)
Open ALL runs (Key and Meter)
Open ALL shutoff’s (@manifold, @pump after check valve, @ return manifold.
Reconnect ALL electronic triggering.
Trigger Basement Zone, On comes MAIN pump, On comes Zone pump water starts to circulate (AXIOM is on and pressure topped up and water level tank goes down)
Run 10 min.
Check flow metres and can’t tell if working
I know I have flow because AXIOM did its job, if I open relief valve (at top of system)
Water comes out and pressure drops and AXIOM kicks on.
CONTACT WATTS.
Email back and forth with tech department in BC (I still have emails I think, will look for them and forward to you)
 
I did other zones and had same issue. I now realize that there was nothing wrong with the flow meters they were just not sensitive enough to pickup 1/16th to 1/8th gpm flow.
 
I found this out after experimentation and turning on boiler to heat water.
 
Had no choice but to tough it out over the winter
I was lucky that the house stayed warm due to R66 ceilings, R32 walls and ICF foundation. Thermal blinds and Thermal drapes. 1900 sq ft. bungalow.
80,000 Btu boiler electric 4 stage 5.5KW elements. Average power consumption was 6 to 10KW/H 0 to -25C outside. (as per hydro datat) However, some of this additional power was due to use of 2 -1.5KW heaters as supplementary heat on coldest sunless days.
 
LAST winter the system ran as follows.
Basement zone 8runs. 1 run ON 7 OFF ¾ to 1 gpm/ 8 run ON / flow by 8 (not readable)
Ended up using 4 outside RUNS down to 2 when it got cold.
Alternated other two zones which are upstairs and divided up runs to outside.
In other words, a lot of manipulation to keep house at 18C on cold days.
 
So you see I was hoping to have found my answer by now, but life has a way of getting in the way. So here I am back at it before winter starts.
 
I can get the same performance as last year but I need way better.
 
My problem assumes the following when sizing pump.
 
All circulator pumps are typically sized based on the heat load and head loss (pressure drop) for a given zone.
  1. Knowing the heat load (in BTU's) for a given zone, allows to calculate the required circulator pump's flow rate in gallons per minute (GPM).
 
For hot water hydronic or radiant heating applications, the following equation can be used:
 
GPM = 0.002*BTU/(Temperature Drop, F),


where Temperature Drop is the difference between supply and return temperatures in the system and GPM is the amount of flow the circulator must produce.
 
Since most of the radiant heating systems utilize a 20F temperature drop, the formula can be changed to:
 
1 GPM = 10,000 BTU/hr,
 
meaning that for every 10,000 BTU's of heat load the circulator must output a 1 gallon per minute flow.
 
This  system calls for 80,000 BTU/hr, circulator pump should have a minimum 8 Gallons Per Minute flow rate at a given pressure drop.
 
  1. The next step is to calculate the head loss, or pressure drop in the system.
 
Head loss is associated with friction of the water against the internal surface of the pipes/tubing in the hydronic or radiant heating system and restricts flow rate a circulator can produce.
Although radiant heat manifold and PEX tubing sizing are a different topic, this systems manifold has 8 outlets with 1/2" PEX tubing installed at 250ft length per loop and the system calls for 80,000 BTU's.
Using the formula above, we can determine the flow rate required for our given zone: 80,000/10,000 = 8.0 GPM.
Flow rate through every selected circuit of the manifold equals Flow Rate divided by number of Circuits:
8 GPM/8 circuits = 1 GPM per circuit (assuming that the circuits are equally balanced).
Using a Pressre Drop Table or Pressure Drop Chart, supplied by the PEX tubing manufacturer, a pressure drop per ft of tubing can be calculated at a given GPM flow rate.
NOTE: Pressure drop data supplied by manufacturers may be available both in PSI (lbs per square inch) and in foot (ft) of head.
For conversion, I used the following equation: 1 psi = 2.3 ft of head (for fresh water), and 1 ft of head = 0.43 psi
In this example, pressure drop per 1 ft of 1/2" PEX tubing at 1 GPM flow rate would be approximately 0.03 ft of head).
Considering that each individual PEX tubing circuit is 250 ft long, pressure drop per circuit would be 0.03 x 250 = 7.5 ft of head.
Since PEX tubing circuits are in parallel to each other, pressure drop per circuit is always the same as the total zone pressure drop. So, the total pressure drop is: 7.5 ft of head
We now have the complete specification for the circulator pump available: 8 GPM flow at 7.5 ft of head pressure drop.
I understand that other components installed within a given zone (such as the radiant heat manifold itself, fittings, check valves, mixing valves, balancing valves, heat exchangers, PEX tubing length (different diameters), etc.) also have to be considered when sizing a circulator pump (see Scheme 1 below). Pressure drop information is usually available in a form of technical specifications or submittal sheet supplied by the manufacturer. Given real conditions, we may add extra 2 ft of head just in case, making pressure drop 9ft of head.                    NOTE: Pump head is a term used to describe the force the circulator develops to overcome pressure drop (pipe, fittings and valves). In a Closed System, "pump head" is NOT the height of the building. Height (on the Scheme above) is not taken into consideration. Regardless of this the zone manifold is below the pump, only rise is as pex comes out of top of pump to curve around and down to manifold. As per pics
  1. The next and final step, is to match the obtained data with a correct pump on a Circulator Pump Curve Chart  Which should be the Grundfos 15*58 on mid speed??????
But it is not the case.

Hope you can help, i'm not sure if the pump is functioning properly, from startup last winter it has never pushed what i had hoped it would.
AGAIN
Its not that it does not work, it is that it does not provide what the specs said it would. I have another system i did and i had no problems with that but it was hooked to a potable town water.
This system is on a pressure/fill tank which provides a system pressure of 12 psi on input to pump.

I have same ups15-58 on another system and it gives me 4 gpm to manifold no problem (.5gpm per run)

thanks neil
ronmarUser is Offline
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09 Oct 2015 05:27 PM
Neil
Your writeup references pics and schematics... Where can we see those?
chingoUser is Offline
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11 Oct 2015 07:54 AM
the forum has a max. size of 100kb so i can't upload any pics.
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11 Oct 2015 11:21 AM
Posted By chingo on 11 Oct 2015 07:54 AM
the forum has a max. size of 100kb so i can't upload any pics.
You just have to reduce the size of the pics.

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11 Oct 2015 01:54 PM
Or put them up on photobucket (free account/access) or some other hosting site and put a link to them here, like this. We can talk about it all day, but your most detailed description isn't going to show us the checkvalve or pump that is installed backwards:)

[URL=http://s270.photobucket.com/albums/jj85/rmarlett/?action=view¤t=1ecd26aa.jpg][/URL]
chingoUser is Offline
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11 Oct 2015 04:11 PM
hopefully my pic uploaded. checked all manifolds and flow is same on input as output. Flow meters measured .5gpm on loops(runs) and approx 4gpm if you add them up. I then took hose return back to purge cart out and filled a bucket, after 60 sec. the measured water was approx. 4gpm. Therefore Manifold has no restriction to flow under these conditions. Brings me back to something in my main system. I will post pics of this.
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11 Oct 2015 04:16 PM
pic
ronmarUser is Offline
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11 Oct 2015 07:09 PM
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chingoUser is Offline
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12 Oct 2015 08:09 AM
manifold
NRT.RobUser is Offline
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12 Oct 2015 08:17 AM
Any chance a pump is in backwards or supply/return backwards at the manifold? I've seen that more than once Flow meter manifolds don't like that much.
Put the 15-58 on speed 3 and make sure it's correctly seated in the 3 position and not slightly in between.
Not sure what your piping looks like but you could try removing any internal checks. At the very least you could inspect the intake of the pump and make sure you don't have any blockage.

Just a couple of simple starting points.
Rockport Mechanical<br>RockportMechanical.com
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12 Oct 2015 08:34 AM
more pics pres/fil tank
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12 Oct 2015 08:34 AM
main loop
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12 Oct 2015 08:36 AM
Watts radiant heating system. 3 zones all exhibiting same issue. Purged with 1 hp submersible pump.(manifolds done individually, the main loop, then combined) 1 zone 8 loop manifold same elevation as main loop (all runs 250' 1/2" pex) 1 zone 8 loop manifold 6 ft above main loop (all runs 250' 1/2" pex) 1 zone 4 loop manifold 6 ft above main loop (all runs 250' 1/2" pex) All pumps Grundfos UPS 15-58 set to med. Calculated head .03 * 250 = 7.5 ft of head On pump curve that gives a flow rate of approx. 7-8gpm. Test on Zone same level as main loop. 8runs ACTUAL test results using 1HP open loop injected between exp tank/bubbler = 3.2gpm total (approx. .4gpm run) ACTUAL test results using 1HP open loop injected directly into manifold = 4.1gpm total (approx. .5gpm run) ACTUAL test results using UPS15-58 closed loop 12psi. @manifold .75 gpm toatl (approx. .08gpm run) Hi speed very little improvement. Change to UPS 26-99 very little improvement. Other zones exhibiting same characteristics. Thankyou for your time and any help you may be in this issue. Neil
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12 Oct 2015 08:37 AM
Just to be sure, you're aware that you appear to have the return leg valved off in that pic? And you will need checks on this system so don't take them out (but do inspect them if you haven't).
Rockport Mechanical<br>RockportMechanical.com
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12 Oct 2015 08:38 AM
Disregard isolation levers. One in pic main loop set to purge zone. Turned on will purge main loop.
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12 Oct 2015 08:40 AM
It is strange that ALL 3 zones are exhibiting same reduced flow from calculations.
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12 Oct 2015 08:40 AM
If all 3 have the same issue it's probably not blockage at the pump. Could be obstruction at the tempering valve though. that's unusual but it does happen.
Rockport Mechanical<br>RockportMechanical.com
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