|
Water Flow Chart #1 The chart below takes into consideration the potential damage from hydraulic hammer (shock) and noise considerations due
to excessive fluid velocity. You can flow more than what is shown in the chart (see Chart #2 below) however, you may run into problems if you do.
|
|
|
Assume Gravity to Low Pressure. About 6f/s flow velocity, also suction side of pump |
Assume Average Pressure. (20-100PSI) About 12f/s flow velocity |
Assume "High Pressure" PEAK flow. About 18f/s flow velocity* |
| Sch 40 Pipe Size |
ID
(range) |
OD |
GPM
(with minimal pressure loss & noise) |
GPH
(with minimal pressure loss & noise) |
GPM
(with minimal pressure loss & noise) |
GPH
(with minimal pressure loss & noise) |
GPM
(with significant pressure loss & noise) |
GPH
(with significant pressure loss & noise) |
| 1/2" |
.50-.60" |
.85" |
7 gpm |
420 gph |
14 gpm |
840 gph |
21 gpm |
1,260 gph |
| 3/4" |
.75-.85" |
1.06" |
11 gpm |
660 gph |
23 gpm |
1,410 gph |
36 gpm |
2,160 gph |
| 1" |
1.00-1.03" |
1.33" |
16 gpm |
960 gph |
37 gpm |
2,220 gph |
58 gpm |
3,510 gph |
| 1.25" |
1.25-1.36" |
1.67" |
25 gpm |
1,500 gph |
62 gpm |
3,750 gph |
100 gpm |
5,940 gph |
| 1.5" |
1.50-1.60" |
1.90" |
35 gpm |
2100 gph |
81 gpm |
4,830 gph |
126 gpm |
7,560 gph |
| 2" |
1.95-2.05" |
2.38" |
55 gpm |
3300 gph |
127 gpm |
7,650 gph |
200 gpm |
12,000 gph |
| 2.5" |
2.35-2.45" |
2.89" |
80 gpm |
4800 gph |
190 gpm |
11,400 gph |
300 gpm |
17,550 gph |
| 3" |
2.90-3.05" |
3.50" |
140 gpm |
8400 gph |
273 gpm |
16,350 gph |
425 gpm |
25,650 gph |
| 4" |
3.85-3.95" |
4.50" |
240 gpm |
14,400 gph |
480 gpm |
28,800 gph |
700 gpm |
42,000 gph |
| 5" |
4.95-5.05" |
5.563" |
380 gpm |
22,800 gph |
750 gpm |
45,000 gph |
1100 gpm |
66,000 gph |
| 6" |
5.85-5.95" |
6.61" |
550 gpm |
33,000 gph |
1100 gpm |
66,000 gph |
1700 gpm |
102,000 gph |
| 8" |
7.96" |
8.625" |
950 gpm |
57,000 gph |
1900 gpm |
114,000 gph |
2800 gpm |
168,000 gph |
Water Flow Chart #2
Here is yet another set of data predicting the amount of flow through a straight piece of pipe. If you add any direction change (90's, 45's Tees, Wyes, etc) or potention restrictions (valves, elevation change, obstruction, etc) these estimates will also change.
| Pressure | Flow in GPM through pipe ID in inches |
| PSI | 1" | 1.25" | 1.5" | 2" | 2.5" | 3" | 4" | 5" |
| 20 | 26 | 47 | 76 | 161 | 290 | 468 | 997 | 2895 |
| 30 | 32 | 58 | 94 | 200 | 360 | 582 | 1240 | 3603 |
| 40 | 38 | 68 | 110 | 234 | 421 | 680 | 1449 | 4209 |
| 50 | 43 | 77 | 124 | 264 | 475 | 767 | 1635 | 4748 |
| 60 | 47 | 85 | 137 | 291 | 524 | 846 | 1804 | 5239 |
| 75 | 53 | 95 | 153 | 329 | 591 | 955 | 2035 | 5910 |
| 100 | 62 | 112 | 180 | 384 | 690 | 1115 | 2377 | 6904 |
| 125 | 70 | 126 | 203 | 433 | 779 | 1258 | 2681 | 7788 |
| 150 | 77 | 139 | 224 | 478 | 859 | 1388 | 2958 | 8593 |
| 200 | 90 | 162 | 262 | 558 | 1004 | 1621 | 3455 | 10038 |
Water Flow Chart #3
Below is another data set we've run across. What is shows is how much flow you will get across a stainless metal ball valve of the length specified with a 1PSI pressure drop from one side of the valve to the other.
| Size (ID, inches) | Length (inches) | Flow (GPM) |
| 1/2 | 4.25 | 26 |
| 3/4 | 4.62 | 50 |
| 1 | 5.00 | 94 |
| 1-1/2 | 6.50 | 260 |
| 2 | 7.00 | 480 |
| 2-1/2 | 7.50 | 750 |
| 3 | 8.00 | 1300 |
| 4 | 9.00 | 2300 |
| 6 | 15.50 | 5400 |
Note: The data is for water through the valve only, and does not take into account the rest of the system. It does not give flow velocity, so there is some question as to the applicability of the data. The data comes from a book for industrial piping and probably assumes a massive pump, high flow velocities and metallic pipes. (Ie, where water hammer and noise are less of a concern than with PVC pipe.) As always, "you mileage may vary."
|
|
GPM/GPH Flow based on PVC Pipe Size
There are now 3 charts and one formula on this page showing water flow through a pipe. These 3 charts come from 3 different sources, and they all are just general guidelines. and should not be relied on as a precise source for information or as a substitute for engineering. The data between them does vary. In the chart to the left is a general guideline for how much liquid a pipe of specific size can flow in GPM (Gallons Per Minute) & GPH (Gallons Per Hour.) There are three columns. (Well there are really six, but each colum is shown in Gallons per minute, and then again as Gallons per Hour.) The first set of columns would be the minium you would expect for the pipe size shown using nothing but gravity in a low head pressure situation to power the flow. The 2nd set of columns show what you can expect using an average pump with a pressure from 20 to 100psi. The 3rd set of columns is the maximum flow based on maximum recommended velocity of the liquid in the pipe. You may exceed this, but you will have to contend with excessive noise and exceedingly high inertial impacts. (I.e. Possible system failure due to hydraulic hammer effects.) This is a very general guide and is subject to many variables. Pressure, noise allowance, bends, fittings, viscosity, etc. affect how much liquid will flow through a pipe of given size. If you can accept more noise and have higher pressure, you can pump more at the risk of system failure. If you have a lot of bends and fittings you will flow less. The flow rates shown should not produce unacceptable noise, however, many variables affect noise, so this is no guarantee that the system will be noiseless. Sometimes experimentation is the only sure way to know if a system will be noisy or not. The flow rates shown are for water, with viscosity of 1. Higher viscosity liquids will flow less, lower viscosity liquids may flow more. You can use the Hazen-Williams equation below to calculate the exact flow loss through a pipe.
Friction Loss
If you really want to get technical and calculate the exact friction loss through PVC and CPVC pipe you can use the Hazen-Williams equation as expressed below for water:
f = 0.2083 (100/c)1.852 q1.852 / dh4.8655
where
f = friction head loss in feet of water per 100 feet of pipe (fth20/100 ft pipe)
q = volume flow (gal/min)
dh = inside diameter (inches)
c = a constant for internal pipe roughness. 150 is the commonly accepted value for PVC and CPVC pipe.
You can also print out and use the Nomograph courtesy of Plastics Pipe Institute, a division of The Society of
The Plastics Industry. (Note: You normally want to keep your flow velocity under 12 feet per second for 4" and under and 5 feet/second for 5" and above to avoid hydraulic shock.)
What about fittings? How do they effect flow? See our Friction loss due to pvc pipe fittings chart.
Compared to other materials on construction for pipe, thermo-plastic pipe smoothness remains relatively constant throughout its service life.
If you are flowing something other than water, you'll have to adjust the formula for the viscosity of the liquid you are flowing.
Note: One of the benefits of using Flex PVC pipe is being able to make long gradual bends instead of using fittings which will allow more flow with less noise, less back pressure, and less load on the pump. In other words, a more efficient system.
*"High Pressure" is a general and non-specific figure. What might be "high pressure" for 1/2" pipe (600psi) may not be "high pressure" for 2" pipe (280psi). There are just too many variables to consider to give a real world number. The fact of the matter is, on a pressurized system, the pump will dictate the flow and pressure as much as the pipe used. To achieve the flow figures in the peak column, it's assuming there are no bends and a short straight flow path. If your system has bends and T's, Wyes, etc, you should go to a larger pipe to achieve the flow desired. Also feed pressure effects the system. If the feed pressure is too low, you can get cavitation and you'll damage the pump and flow very little.
|
Follow us on Twitter for news, sales, & discounts.
