Filter capacity?

Are you saying that the entire flow is being put through a 1" PVC pipe?

If yes, then this needs to be fixed as that is way too small for the flow.

I really do not think that that is something that anyone would do.

Are you sure?

How long is the 1" pipe?
Here is the section the technician is referring to. The "T" connects pipe coming out of both filters. At the first 90, there is about 28" of 1" pipe. At the second 90, there is about 12" of 1" pipe.
 

Attachments

  • IMG_5173.jpg
    IMG_5173.jpg
    244.4 KB · Views: 6
  • IMG_5174.jpg
    IMG_5174.jpg
    214 KB · Views: 6
  • IMG_5175.jpg
    IMG_5175.jpg
    291.2 KB · Views: 6
If the $500 cost to clean each heater is in addition to the service contract cost it is laughable. Most HVAC clean and check costs are normally between $100-120 with many companies offering a clean and check at $70-80 to get their foot in the door. The manufacturer's recommendation of annual cleaning is more of a liability issue and may only be needed when a heater is installed in a location where it gets dirty very quickly or is highly attractive to spiders. Although an annual clean and check can catch some small problems before they become a larger problem.
Do these prices seem high also? Contract says they do these things between September and March unless notified otherwise.
  • Test and Calibrate VGB Anti-Entrapment Device (To be done at opening) $ 100.00 per device
  • Re-Condition Chemicals Feeders (Will be picked up during closing) $ 100.00 + materials
  • Clean DE & Cartridge Filters: Association Has __2____ $ 200.00 each (we actually on have 1 DE filter)
  • Clean Pool Heater (per manufacturer’s recommendations) $ 500.00 for 125 – 405BTU
 
All pipe is marked with the size.

See what size the pipe is.

Are you saying that only half of the flow goes through the smaller pipe and that the T is a 3" T?

1694288608227.png
 

Attachments

  • 1694288726015.png
    1694288726015.png
    183.1 KB · Views: 2
The regulations usually require that the velocity for suction remain below 6 feet per second and below 8 feet per second for the returns.

I really doubt that anyone would try to put 170 GPM through a 1" PVC pipe.

You want to keep the water velocity below 6 ft/sec on the suction and below 8 ft/sec on the pressure side of the pump.


Pipe Size6 ft/sec8 ft/sec
1.5"38 GPM51 GPM
2"63 GPM84 GPM
2.590 GPM119 GPM
3.0"138 GPM184 GPM
4.0"235 GPM312 GPM
If the pipes are 2", then they can carry up to 84 GPM each for a total of 168 GPM.

You cannot have a velocity in any suction pipe higher than 6 feet per second and you cannot have a velocity higher than 8 feet per second in any return line.

If the velocity is excessive, it needs to be fixed.
 

1694289290439.png

ANSI/APSP/ICC-1 2014 American National Standard for Public Swimming Pools​




1694289471352.png

1694289542297.png




ANSI/PHTA/ICC-2 2023 American National Standard for Public Pool and Spa Operations and Maintenance​


1694289824355.png



ANSI/PHTA/ICC-7 2020 American National Standard for Suction Entrapment Avoidance in Swimming Pools..​



ANSI/APSP/ICC-11 2019 American National Standard for Water Quality in Public Pools and Spas​

 
TITLE 77: PUBLIC HEALTH
CHAPTER I: DEPARTMENT OF PUBLIC HEALTH
SUBCHAPTER n: RECREATIONAL FACILITIES
PART 820 SWIMMING FACILITY CODE
SECTION 820.210 SWIMMING FACILITY WATER TREATMENT SYSTEM​



Section 820.210 Swimming Facility Water Treatment System

a) General Requirements

1) A water treatment system, consisting of pumps, piping, filters, water conditioning, disinfection equipment and other accessory equipment shall be provided to clarify, chemically balance and disinfect the swimming pool water. The system shall be designed for a recirculation flow rate that will result in a turnover period in each pool not exceeding those specified below. Systems serving pools with skimmers shall be designed for a flow rate of at least 30 gallons per minute for each skimmer.

Type of Pool​
Maximum Turnover Period
Diving Pools
8 Hours​
Wading Pools, Wading Areas
2 Hours​
Plunge Pools and Plunge Areas for Water Slides
2 Hours​
Lazy Rivers
2 Hours​
Other Pools
6 Hours​
Spas
30 Minutes​

I don't see any place in the Code where it says the flow rate may be reduced when bathers are not present and have been told on several occasions that the required flow rate must be maintained at all times.
 
My apologies.... definitely 2" pipe the technician thinks is restricting flow (not 1") and thinks should be replaced with 3" pipe. He wants to connect the two 2" pipes coming out of the filters to a 3" T and replace 2 sections (about 40" total) of 2" pipe with 3" pipe and will also include two 3" elbows. See attached pics.

Do you agree that that work would probably help increase the flow rate?

Also.... see arrow on pump. I can confirm it is spinning in the right direction. I think we can put that issue to rest.
 

Attachments

  • IMG_5206.jpg
    IMG_5206.jpg
    235.9 KB · Views: 4
  • IMG_5204.jpg
    IMG_5204.jpg
    248.6 KB · Views: 4
  • IMG_5203.jpg
    IMG_5203.jpg
    223.2 KB · Views: 5
  • IMG_5202.jpg
    IMG_5202.jpg
    240.3 KB · Views: 5
  • IMG_5201.jpg
    IMG_5201.jpg
    273.5 KB · Views: 5
  • Like
Reactions: JamesW
It looks like you are correct.

In my opinion, it is ridiculous to keep the pump running at 167 GPM 24/7.

It is a huge waste of energy.

However, if it is the law, then I am not going to say to do otherwise.


1694297054682.png




1694297268546.png
 

Enjoying this content?

Support TFP with a donation.

Give Support
The 2" pipes coming out of the filters are ok as long as they T into a 3" T.

A 2" pipe can take up to 84 GPM each for a total of 168 GPM.

If the 2" pipes go into a 2" T, then that should be changed.

I would not have more than 8 feet per second in the return lines.

Actually the code says 10 feet per second, but I would try to stick to 8 feet wherever possible.

B) The piping shall be designed to carry the required flow at velocities not exceeding 5 feet per second in suction piping, and 10 feet per second in pressure piping, unless greater velocities can be hydraulically provided.


1694298076016.png

 
The 2" pipes coming out of the filters are ok as long as they T into a 3" T.

A 2" pipe can take up to 84 GPM each for a total of 168 GPM.

If the 2" pipes go into a 2" T, then that should be changed.

I would not have more than 8 feet per second in the return lines.

Actually the code says 10 feet per second, but I would try to stick to 8 feet wherever possible.
So what the technician is telling me makes sense.... that the 2" pipes coming out of the two filters should connect into a 3" T... and that should connect to 3" pipe and elbows throughout the return line.... instead of it connecting to a 2" T and 40 inches of 2" pipe before it goes into 3" pipe. Is that correct? He was puzzled as to why anyone would have plumbed it that way in the first place. If that section of the plumbing is corrected, do you have a guess on how much our flow might increase?
 
  • Like
Reactions: JamesW
Request a copy of the places monthly electrical bill. That will show you the cost/kwh and all other surcharges per kwh.
I looked at my own electric bill this past month and divided the total bill for the month by the total kw hours used and got 13.50 cents per kwh. So here's my calculation to run our outdoor pump for the season:

3.7 x .1350 x 24 = $11.98 per day x 112 days (16 week season) = $1,342.66. So.... about $1,350 to run the pump for the season. Sound about right?

I assume I could use the same formula to get the cost of running our indoor pump... Check the pump label for KW on the label (which will be lower since it's a smaller pump), but multiply the daily rate I calculate by by 365 since it runs all year long. Sound right?
 
Last edited:
  • Like
Reactions: JamesW
If that section of the plumbing is corrected, do you have a guess on how much our flow might increase?
10 feet of 2" pipe (equivalent) creates about 5.76 feet of head loss at 180 GPM, which is about 2.49 psi.

10 feet of 3" pipe (equivalent) creates about 0.801 feet of head loss at 180 GPM, which is about 0.347 psi.

The difference will be about 4.96 feet of head or 2.14 psi, so the flow will improve by about 2 GPM.

1694346815685.png
 
Last edited:
10 feet of 2” PVC has a curve of about 0.00017778X^2.

10 feet of 3” PVC has a curve of about 0.00002472X^2.

If the system has a curve of 0.00246914X^2 with the 10’ of 2” PVC, the new system will be 0.00246914 - 0.00017778 + 0.00002472 = 0.00231608X^2.

0.00231608/0.00246914= 0.938 = 93.8%

If the old operating point was 80 feet of head at 180 GPM, the new operating point will be about 182 GPM at about 76.7 feet of head.

So, you should gain about 2 GPM and the pressure should go down by about 1.4 psi.

You might, or might not, see a difference in the flow.

In my opinion, the flow is somewhat uncertain as we are getting two different readings.

However, the higher flow is more consistent with the pump performance curve assuming the pump is working as expected.

1694351121600.png
 
Last edited:
2" PVC does create a restriction, but not as much as people might think.

For 10' of 2" PVC at 200 GPM, the velocity is about 20.4 feet per second and the head loss is about 7 feet or about 3 psi.


1694353043829.png


1694352973326.png






1694353294264.png


 
In the picture, you can see that the total HP is listed as 2.2.

The kW is usually = to the total HP, not the label HP.

2.2 total HP = 2.2 kw.

2.2 x 0.1350 = $0.297 (per hour) x 24 hours = $7.128 (per day) x 365 days = $2,601.72 per year

Per week = $50.03. Per month = $216.81.

Also, the volts x amps = watts.

230 x 10.4 = 2,392 watts.

That is the maximum power the pump should ever be loaded to.

However, the actual load is usually lower by maybe 5 to 10%.

0.92 x 2,392 = 2,200 watts.

img_5207-jpg.529247
 

Enjoying this content?

Support TFP with a donation.

Give Support
Thread Status
Hello , This thread has been inactive for over 60 days. New postings here are unlikely to be seen or responded to by other members. For better visibility, consider Starting A New Thread.