Ind. Admin. Code tit. 410, r. 6-8.3-76
Authority: IC 16-19-3-4
Affected: IC 16-19-3-4
Sec. 76. (a) Subsurface trench flood dosed on-site sewage systems shall meet all of the requirements of:
(b) When a subsurface trench flood dosed soil absorption system is used, the dosing effluent pump shall be sized, and its controls set to deliver the DDF to the soil absorption field in each dose. Effluent pump selection shall be based on manufacturer's pump curves for the required discharge rate from Table VII, as follows, at the total head imposed on the pump:
| Table VII – Required Effluent Pump Discharge Rates for Subsurface Trench Flood Dosed On-Site Sewage Systems | |
| Number of Bedrooms | Discharge Rate in Gallons per Minute |
| 1 | 30-35 |
| 2 | 30-35 |
| 3 | 30-45 |
| 4 | 30-60 |
| 5 | 38-75 |
| 6 | 45-90 |
(c) The total head for a subsurface trench flood dosed soil absorption system shall be the elevation difference between the effluent pump off and the highest point in the force main or the outlet of the effluent force main in the distribution box, whichever is the highest elevation, in addition to the friction loss in the effluent force main expressed in feet.
(d) The effluent force main shall drain unless it is installed below the frost line, as listed in Table VIII, as follows, and designed so that no effluent remains in any portion of the effluent force main located above the frost line:
| Table VIII – Frost Penetrations in Indiana (in inches) | |||||||
|---|---|---|---|---|---|---|---|
| Adams | 60 | Franklin | 48 | Lawrence | 48 | Rush | 54 |
| Allen | 60 | Fulton | 60 | Madison | 60 | St. Joseph | 60 |
| Bartholomew | 48 | Gibson | 42 | Marion | 54 | Scott | 36 |
| Benton | 60 | Grant | 54 | Marshall | 60 | Shelby | 54 |
| Blackford | 60 | Greene | 54 | Martin | 48 | Spencer | 36 |
| Boone | 54 | Hamilton | 54 | Miami | 60 | Starke | 60 |
| Brown | 48 | Hancock | 54 | Monroe | 48 | Steuben | 60 |
| Carroll | 60 | Harrison | 36 | Montgomery | 60 | Sullivan | 54 |
| Cass | 60 | Hendricks | 54 | Morgan | 48 | Switzerland | 42 |
| Clark | 36 | Henry | 54 | Newton | 60 | Tippecanoe | 60 |
| Clay | 54 | Howard | 60 | Noble | 60 | Tipton | 60 |
| Clinton | 54 | Huntington | 60 | Ohio | 42 | Union | 48 |
| Crawford | 36 | Jackson | 48 | Orange | 42 | Vanderburgh | 36 |
| Daviess | 48 | Jasper | 60 | Owen | 54 | Vermillion | 60 |
| Dearborn | 48 | Jay | 60 | Parke | 60 | Vigo | 60 |
| Decatur | 48 | Jefferson | 42 | Perry | 36 | Wabash | 60 |
| Dekalb | 60 | Jennings | 48 | Pike | 42 | Warren | 60 |
| Delaware | 60 | Johnson | 54 | Porter | 60 | Warrick | 36 |
| Dubois | 42 | Knox | 48 | Posey | 42 | Washington | 36 |
| Elkhart | 60 | Kosciusko | 60 | Pulaski | 60 | Wayne | 54 |
| Fayette | 54 | LaGrange | 60 | Putnam | 54 | Wells | 60 |
| Floyd | 36 | Lake | 60 | Randolph | 54 | White | 60 |
| Fountain | 60 | LaPorte | 60 | Ripley | 48 | Whitley | 60 |
(e) In addition to the liquid holding capacity of a dosing tank stated in section 62(f) of this rule the following shall apply:
(f) The distal end of the effluent force main in the distribution box must be fitted with an elbow turned down or a sanitary tee, or else the distribution box must be baffled.
(g) The minimum inside diameter of the effluent force main shall be one (1) inch. The maximum inside diameter of the effluent force main shall be four (4) inches.
(h) Tables IX and X, as follows, shall be used in determining friction losses in the effluent force mains and manifold when plastic pipe is used:
| Table IX – Friction Losses in Plastic Pipe (per 100 feet of pipe) | ||||||||||||||
| Pipe Diameter, Flow (gpm), Velocity (v)2, and Friction Loss Head (Hf)1 | ||||||||||||||
| Flow (gpm) | 1" | 1 1/4" | 1 1/2" | 2" | 2 1/2" | 3" | 4" | |||||||
| Q | v | Hf | v | Hf | v | Hf | v | Hf | v | Hf | v | Hf | v | Hf |
| 1 | 0.37 | 0.11 | ||||||||||||
| 2 | 0.74 | 0.38 | 0.43 | 0.10 | ||||||||||
| 3 | 1.11 | 0.78 | 0.64 | 0.21 | 0.47 | 0.10 | ||||||||
| 4 | 1.49 | 1.31 | 0.86 | 0.35 | 0.63 | 0.16 | ||||||||
| 5 | 1.86 | 1.92 | 1.07 | 0.52 | 0.79 | 0.24 | ||||||||
| 6 | 2.23 | 2.70 | 1.29 | 0.71 | 0.95 | 0.33 | 0.57 | 0.10 | ||||||
| 8 | 2.97 | 4.59 | 1.72 | 1.19 | 1.26 | 0.56 | 0.77 | 0.17 | ||||||
| 10 | 3.71 | 6.90 | 2.15 | 1.78 | 1.58 | 0.83 | 0.96 | 0.25 | 0.67 | 0.11 | ||||
| 15 | 5.57 | 14.7 | 3.22 | 3.76 | 2.37 | 1.74 | 1.43 | 0.52 | 1.01 | 0.22 | ||||
| 20 | 7.43 | 25.2 | 4.29 | 6.42 | 3.16 | 2.96 | 1.91 | .87 | 1.34 | 0.37 | 0.87 | 0.13 | ||
| 25 | 9.28 | 38.6 | 5.37 | 9.74 | 3.94 | 4.46 | 2.39 | 1.29 | 1.68 | 0.54 | 1.09 | 0.19 | ||
| 30 | 6.44 | 13.6 | 4.73 | 6.27 | 2.87 | 1.81 | 2.01 | 0.76 | 1.30 | 0.26 | ||||
| 35 | 7.51 | 18.2 | 5.52 | 8.40 | 3.35 | 2.42 | 2.35 | 1.01 | 1.52 | 0.35 | 0.88 | 0.10 | ||
| 40 | 8.59 | 23.6 | 6.30 | 10.7 | 3.83 | 3.12 | 2.68 | 1.28 | 1.74 | 0.44 | 1.01 | 0.12 | ||
| 45 | 7.09 | 13.5 | 4.30 | 3.85 | 3.02 | 1.54 | 1.95 | 0.55 | 1.13 | 0.15 | ||||
| 50 | 7.88 | 16.5 | 4.78 | 4.68 | 3.35 | 1.93 | 2.17 | 0.67 | 1.26 | 0.18 | ||||
| 60 | 9.47 | 23.6 | 5.74 | 6.62 | 4.02 | 2.72 | 2.60 | 0.94 | 1.51 | 0.25 | ||||
| 70 | 6.70 | 8.86 | 4.69 | 3.67 | 3.04 | 1.25 | 1.76 | 0.33 | ||||||
| 80 | 7.65 | 11.5 | 5.36 | 4.69 | 3.47 | 1.59 | 2.02 | 0.42 | ||||||
| 90 | 8.60 | 14.3 | 6.03 | 5.83 | 3.91 | 1.99 | 2.27 | 0.52 | ||||||
| 100 | 6.70 | 7.13 | 4.34 | 2.42 | 2.52 | 0.63 | ||||||||
| 125 | 8.38 | 10.9 | 5.43 | 3.72 | 3.15 | 0.96 | ||||||||
| 150 | 6.51 | 5.16 | 3.78 | 1.34 | ||||||||||
| 175 | 7.60 | 6.90 | 4.41 | 1.79 | ||||||||||
| 200 | 8.68 | 8.93 | 5.04 | 2.27 | ||||||||||
| 225 | 5.67 | 2.84 | ||||||||||||
| 250 | 6.30 | 3.37 | ||||||||||||
| 275 | 6.93 | 4.13 | ||||||||||||
| 300 | 7.56 | 4.87 | ||||||||||||
| 325 | 8.19 | 5.70 | ||||||||||||
| 1 This figure is based on flows for PVC Schedule 40 pipe (flow coefficient: C-150). Other values for friction loss may be used if documentation from the pipe manufacturer is provided with the plan submittal. Calculations using the Hazen-Williams equation may be used if provided with the plan submittal. | ||||||||||||||
| 2 Flow velocity must be at least 2 fps; flow velocities above 5 fps should be avoided. | ||||||||||||||
| Table X - Plastic Pipe Fittings: Friction Loss - Equivalent Length of Straight Pipe (ft.)* | |||||||
| Fitting: | 1" | 1 1/4" | 1 1/2" | 2" | 2 1/2" | 3" | 4" |
| 90° elbow, standard sharp, inside radius | 5.3 | 6.7 | 7.5 | 8.6 | 9.3 | 11.1 | 13.1 |
| 90° elbow, long sweep radius | 2.5 | 3.8 | 4.0 | 5.7 | 6.9 | 7.9 | 12.0 |
| 45° elbow, standard | 1.4 | 1.8 | 2.1 | 2.6 | 3.1 | 4.0 | 5.1 |
| Tee Flow (run flow) | 1.7 | 2.3 | 2.7 | 4.3 | 5.1 | 6.2 | 8.3 |
| Tee Flow (branch flow) | 6.0 | 7.0 | 8.0 | 12.0 | 15.0 | 16.0 | 22.0 |
| Gate Valve | 0.6 | 0.8 | 1.0 | 1.5 | 1.6 | 2.0 | 3.0 |
| Male/Female adapter | 2.0 | 2.8 | 3.5 | 4.5 | 5.5 | 6.5 | 9.0 |
| *Assigned values. Other values for friction loss may be used if documentation from the pipe manufacturer is provided with the plan submittal. | |||||||
(Indiana Department of Health; 410 IAC 6-8.3-76; filed Oct 19, 2012, 2:06 p.m.: 20121114-IR-410120156FRA; filed Apr 9, 2014, 9:51 a.m.: 20140507-IR-410130350FRA; readopted filed Sep 26, 2018, 2:48 p.m.: 20181024-IR-410180328RFA; readopted filed Nov 14, 2024, 1:24 p.m.: 20241211-IR-410230798RFA)