Nev. Admin. Code § 444.8396 - Pressure distribution system: Design criteria
1. A
pump must be used to pressurize a pressure distribution system. A siphon may be
used in lieu of a pump if adequate elevation head is available. The active
dosing volume must be approximately 10 times the total volume of the
distribution pipe.
2. A solid
delivery pipe which goes from the dosing tank to the perforated distribution
piping must be placed below the frost line. The delivery pipe must maintain a
downward slope from the distribution lines to the dosing tank to ensure that
the line will drain between discharges. Check valves and other devices that
prevent backflow through the pump must not be used so that effluent may, when
necessary, drain back to the dosing tank to protect the pipe from
freezing.
3. To reduce the
potential for plugging and clogging the distribution lines, the diameter of the
discharge hole must be 3/8 inch or more. The rate of discharge for
various-sized holes at various pressures are set forth in the following table:
DISCHARGE RATES AT VARIOUS PRESSURES (gallons per minute) | ||||
Pressure | Hole Diameter | |||
Per Foot of Water | Per Square Inch | 3/8 Inch | 7/16 Inch | 1/2 Inch |
1 | 0.43 | 1.66 | 2.26 | 2.95 |
2 | 0.87 | 2.34 | 3.19 | 4.17 |
3 | 1.30 | 2.87 | 3.91 | 5.10 |
4 | 1.73 | 3.31 | 4.51 | 5.89 |
5 | 2.17 | 3.71 | 5.04 | 6.59 |
4.
Friction losses in schedule 40 plastic pipe are listed in the following table:
FRICTION LOSS IN SCHEDULE 40 PLASTIC PIPE; C = 150 (ft/100 ft) | |||||||||
Pipe Diameter (inches) | |||||||||
Flow in gallons per minute | 1 | 1 1/4 | 1 1/2 | 2 | 3 | 4 | 6 | 8 | 10 |
1 | 0.07 | ||||||||
2 | 0.28 | 0.07 | |||||||
3 | 0.60 | 0.16 | 0.07 | ||||||
4 | 1.01 | 0.25 | 0.12 | ||||||
5 | 1.52 | 0.39 | 0.18 | ||||||
6 | 2.14 | 0.55 | 0.25 | 0.07 | |||||
7 | 2.89 | 0.76 | 0.36 | 0.10 | |||||
8 | 3.63 | 0.97 | 0.46 | 0.14 | |||||
9 | 4.57 | 1.21 | 0.58 | 0.17 | |||||
10 | 5.50 | 1.46 | 0.70 | 0.21 | |||||
11 | 1.77 | 0.84 | 0.25 | ||||||
12 | 2.09 | 1.01 | 0.30 | ||||||
13 | 2.42 | 1.17 | 0.35 | ||||||
14 | 2.74 | 1.33 | 0.39 | ||||||
15 | 3.06 | 1.45 | 0.44 | 0.07 | |||||
16 | 3.49 | 1.65 | 0.50 | 0.08 | |||||
17 | 3.93 | 1.86 | 0.56 | 0.09 | |||||
18 | 4.37 | 2.07 | 0.62 | 0.10 | |||||
19 | 4.81 | 2.28 | 0.68 | 0.11 | |||||
20-24 | 5.23 | 2.46 | 0.74 | 0.12 | |||||
25-29 | 3.75 | 1.10 | 0.16 | ||||||
30-34 | 5.22 | 1.54 | 0.23 | ||||||
35-39 | 2.05 | 0.30 | 0.07 | ||||||
40-44 | 2.62 | 0.39 | 0.09 | ||||||
45-49 | 3.27 | 0.48 | 0.12 | ||||||
50-59 | 3.98 | 0.58 | 0.16 | ||||||
60-69 | 0.81 | 0.21 | |||||||
70-79 | 1.08 | 0.28 | |||||||
80-89 | 1.38 | 0.37 | |||||||
90-99 | 1.73 | 0.46 | |||||||
100-149 | 2.09 | 0.55 | 0.07 | ||||||
150-199 | 1.17 | 0.16 | |||||||
200-249 | 0.28 | 0.07 | |||||||
250-299 | 0.41 | 0.11 | |||||||
300-349 | 0.58 | 0.16 | |||||||
350-399 | 0.78 | 0.20 | 0.07 | ||||||
400-449 | 0.99 | 0.26 | 0.09 | ||||||
450-499 | 1.22 | 0.32 | 0.11 | ||||||
500-599 | 0.38 | 0.14 | |||||||
600-699 | 0.54 | 0.18 | |||||||
700-799 | 0.72 | 0.24 | |||||||
800-899 | 0.32 | ||||||||
900-999 | 0.38 | ||||||||
1000 or more | 0.46 |
5.
Laterals must be spaced so that they are not less than 4 feet or more than 6
feet apart. The outside laterals must be placed at a distance from the
perimeter of the bed that is equal to 1/2 of the distance between the
laterals.
6. Distribution lines in
the pressure distribution system must be looped.
7. The required lateral pipe diameters for
various hole diameters, hole spacings, and lateral lengths for plastic pipe are
shown in the following diagram:
Click here to view image.
8. Manifold diameters for various manifold
lengths, number of laterals, and lateral discharge rates for plastic pipe are
shown in the following diagram:
Click here to view image.
Notes
NRS 439.200, 444.650
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