N13078 - 2014.10.17 - 2 Of 2

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

LOCATION TIME SUB-CATCHMENT RUNOFF INLET DESIGN DRAIN DESIGN HEADLOSSES PART FULL DESIGN LEVELS
tc | | [oo | C [A [GA [AT @ Qg | db tc | | [+a | at [Qn] ds | O | LS vit W2/2g | Ku [ hu | KL |W | Kw | hw | Sf | bf Vp
5 s = |= LE
é z = z= z|2 |8 gl3s 4
2 Bie | 3 5 | 5 7 Z Sie 15 ges 2 5 5 G y
3 = é 2lg.,/ = B\2/=2+/6 = = g 3 Jo/2./35/8 | = giz Suv elu |$8 lg |B a = Sljz2i/1¢6 =| gs
-|2| 2 4 S|£z) 2 lesis./ 2/2) = (Evlsae l28)./2/2) 2] gl) 2) =) 2 /2_|2 Blu | sleele lw 228 S/SL/E J2s/5 | s/ 2/5 [52 B/2 |= se| &
= @ S Se wl fe |SS)| 5 |sS\Gu/ S & 3S /Se|/ssia sal a e az e s| = 5S |S>| Ss z/iz BS |SZ\92r les ee = & > jez’ vlesiae Gi/2z fle ew > Qs = a a =
< ez a & a & 3/22lg2 SE \/eal) Se le#@zeleni7s| = 5 2 la adi yvljPF ee) a;/s/4lz sia =/SZ Ss Ss & 2 BS aSeoea) S&S & |Gea z a = gd wh! &
= 5 a =f 3 Sisyu| = |ZE/ELS| = = w |SS/Zq/SH/TS/ F =z g B55 /=4/ = = welesle« Z €/*sa|>+Slyyisea 5B a E |Sslaciuri¢2s zl se |e eo E |e Pm] 2 Sr e
B) 2) = | 26 |2\ sige] 2 2852/2) 8 | = gelzeis2is3/5\5/2) 22 22/2 2/8 82/8) 2/2 |S ledecsses) 2 & = | s /EPES/ESEs|45| ZlEsies/ =) 3/2/25) 8 |=) a |B8) 2
2 |s2a\e Syise Ss E/Bf| = 2l2%/2/2#/8) 2 /#e\/8e = = 2 @ /£$B/Ls/agleslee #oes/8) 2 i 4 =
By) oo & 28 | 2/4 |22| & Ssies|/ 3/8) 3 e82eis</28| 2) 2)E/ 25 jez eB) & | flf5) 2) | S| F ES|ZE/ESIRS 5 & & B SS|S#\Se(s#/Se) 5 leale#| 8 |S) 8 |s2|/8 |) 5s] 5 jaz) &
yrs % [min {mm/h ha | ha | ha [Ws | Vs % [Vs Us [Us min |mm/h | ha |WVs [Ws [Ws | Vs m % | mm_| m/s _| min m n n m % n n_| m/s n n n n n n
5 G4/D Gu/D Gh 6.00 190 | 088 | 0.84 | 0.065 | 0.055 | 0.055 | 29 0 860 | 161 1 ao Q GO/H 6.00 190 | 0.055 55 2620 6 Fi) 6291 | 100 37513) 0.26 | 0.10 Qg 0.029 Oo 0.029 Do 375 0.003 | 100 | 0.070 100 | 0.070 | 0.03 | 0.002 | 0.103 | 147 | 15.725 | 15.452 | 15.522 15.522 | 16.700 | G4/D
100 to 1/0 6.00 303) 0.88 | 100 | 0.065 | 0.065 | 0.065 | 55 6.00 | 303 | 0.065 (Pipe flow= Grate flow) (159) CHRT 32: Vo2/2gDo 0.01 H/Do 0.00 Upstregm HGL 15.522 below outlet 15.662 | 15.389
FLOW WIDTH/DEPTH 0.651Wd m Kg side flow 10.60 end flow 7.43 pipe oby 15.725
Part full downstream pipe Set Kp fo 1
5 GSE GSE oy 10.00 156 | 083 | 0.79 | 0.252 | 0.199 | 0.199 86 86 860 | 161 1 B B Gt 10.00 | 156 0.199 | 176 | 2620 | 103 B | 2235 | 5.00 37513) 0.66 | 0.04 Qg 0.073 Qo 0.073 De 375 0.022 | 8.96 | 0.199 896 | 0.199 | O17 | 0.006 | O19 | 272 | 15.737 | 15.737 | 15.936 15.936 | 16.682 |  GS/E
100 to 0 10.00 251| 083 | 100 | 0.252 | 0.252 | 0.252 | 176 10.00 | 251 | 0.252 (Pipe flow= Grate flow) (355) CHRT 32: Vo2/2qDo 0.06 H/Do 0.00 15.625 | 15.360
FLOW WIDTH/DEPTH 1,267Wd m Kg side flow 8,96 end flow 6,63
DOWNSTREAM 0,305)
5 vd vd 64,65 6 10.06 | 156 | 0.254 | 220 | 2620 | 123 97 | 16.532 | 4.00 37513) 0.88 | 0.28 Qo 0.097 Do 375 0.039 | 1.00 | 0.073 100 | 0.073 | 0.31 | 0.050 | 0135 | 2.71 | 13.986 | 13.870 | 13.943 13.943 | 16.597 v0
100 to OUT/A 10.06 | 250 | 0.317 (Pipe flow= $um upsty atten flpws) B17) Flow G4/D made eqy grate flow Part full downstream pipe 13.325 | 13.820
Flow G5/E made eqv grate flow Upstream HGL 13943 below outlet
CHRT 32: Vo2/2gDo 0.11 H/Do 0.00 pipe oby 13,986
Kg side flow 7.82 end flow 5.98 Set Kp fo 1
K vals above for stepped pipes as grate flow
5 IN/AA IN/AA IN/S 5.00 202) 082 | 0.78 | 0.100 | 0.078 | 0.078 | 44 hh 050 88 | 1050.05 | bb 0 5.00 | 202 | 0.078 87 997 43 44 | 17.308 | 0.50 OU 235 | 0.12 Og 0.044 Qo 0.044 Do 150 0.281 | 164 | 0.462 164 | 0.462 | 5.12 | 0.885 N46 | 12.215 | 12.677 12.677 | 12.850 | IN/AA
100 to OUT/AA 5,00 321 | 082 0,98 | 0.100 | 0,098 | 0,098 87 5.00 321 0,098 (Pipe flow= Grate flow) (0.73) CHRT 32: Vo2/2qDo 1,82 H/Do 5.17 11330 | 11330
FLOW WIDTH/DEPTH 0.480Wd m Kg side flow 1.64 end flow 1.60
5 G25/AB G25/AB G25 6,00 190 | 088 | 084 | 0,066 | 0,055 | 0,055 ra] 29 258 29% | 108.15 ao 0 6,00 190 0,055 56 2265 2 29 6500 | 0.50 37513) 0.26 On Qg 0,029 Qo 0,029 Do 375 0,003 | 9.71 | 0,033 9.71 | 0.033 | 0.03 | 0.002 7.738 | 7822 | 7.855 71855 | 8376 | G25/AB
100 to G26/AB 6.00 303} 0.88 100 | 0.066 | 0.066 | 0.066 56 6.00 303 0,066 (Pipe flow= Grate flow) (112) CHRT 32: Vo2/2gDo 0.01 H/Do 0,22 7.706 | 7.820
FLOW WIDTH/DEPTH 0.12PWd m Kg side flow 9.71 end flow 6.78
5 G26/AB G26/AB 625,626 6.00 190 | 088 | 0.84 | 0.168 | 0.161 | 0.141 th Th | 44.27 | 296 | 105.15 Th Q 6M 188 0196 | 196 | 1723 9h 02 | 7.182 | 0.50 37513) 0.92 | 0.12 Qg 0.073 Qo 0.102 Do 375 0.063 | 3.10 | 0.134 3.10 | 0.134 | 0.34 | 0.024 | 0.259 | 125 | 7.686 | 7.686 | 7.820 7.820 | 8377 | G26/AB
100 to OUT/AB 6.00 303} 0.88 | 100 | 0.168 | 0.168 | 0.168 | 141 6M 301 | 0.234 [Pipe flow= $um upsty atten flpws) (112) CHART 34 Angle 17 Case 3 7.650 | 1.625
FLOW WIDTH/DEPTH 1:568Wd m $/00 25
Du/Do 1,00 Qg/Qo 0,72 K 2.16
$/Do 1.36 cor 0.94 Ku 3.10 Kw 3.10
5 GVA GVA a 6.00 190 | 088 | 0.84 | 0.358 | 0.301 | 0301 | 159 Bh 150 34 1 85 49 Gt 6.00 190 0301 301 | 1727 | 216 85 | 9370 | 15.00 | 375(3) 0.77 | 0.16 Qg 0.085 Qo 0.085 Do 375 0.030 | 836 | 0.252 836 | 0.252 | 0.24 | 0.022 | 0.090 | 4.20 | 14.731 | 14.731 | 14.983 16,983 | 15.778 | GIA
100 te OUT/B 6.00 303) 0.88 | 100 | 0.358 | 0.358 | 0.358 | 301 ;CrnFL 2 2 | Cen G2/C | 6.00 | 303 | 0.358 (Pipe flow= Grate flow) (6.14) CHRT 32: Vo2/2gDo 0.08 H/Do 0.00 13.325 | 13.060
Kg side flow 8.36 end flow 6.32
FLOW WIDTH/DEPTH 2.72)Wd m
DDWNSTREAM 1.7091
5 Bt GC B 13.00 140 | 083 | 0.79 | 0.096 | 0.076 | 0.076 | 30 2 0.00 189 | 105.107 | 92 0 G2 B00 | 140 | 0.076 60 a a 92 | 5979 | 0.50 37513) 0.83 | 0.10 Qg 0,092 Qo 0,092 Do 375 0.035 | 100 | 0.077 100 | 0.077 | 0.28 | 0.016 | 0.240 | 123 | 16.547 | 16.413 | 14.490 1490 | 15.483 | G3/C
100 to G2/C B00 225 | 0.83 | 100 | 0.096 | 0.096 | 0.096 | 60 B00 | 225 | 0.096 (Pipe flow= Grate flow) (112) CHRT 32: Vo2/2gDo 0.09 H/Do 0.00 Upstregm HGL 14.490 belqw outlet} 4518 | 14.383
FLOW WIDTH/DRPTH 2.128Wd m Kg side flow 8.00 end flow 6.13 pipe oby 14.547
Part full downstream pipe Set Kp fo 1
5 G2/C G2/C 63,62 B00 40 | 0.83 0.79 | 0.433 | 0342 | 0342 | 133 158 0.00 189 | 105.107 | 158 0 B10 Bd 0.418 329 0 at 250 | 3334 | 1100 450(3} 157 0.04 Qg 0.158 Qo 0,250 Do 450 0.126 | 230 | 0.289 230 | 0.289 | 0.77 | 0.026 | 0.158 | 5.02 | 13,767 | 13,767 | 14.056 14.056 | 15.483 G2
100 to OUT/C B00 225 | 0.83 | 100 | 0.433 | 0.433 | 0.433 | 271 B10 | 224 | 0.529 (Pipe flow=| Sum upstream flows) 15.94) Flow G3/C made eqv grate flow CHART 83 Angle jit B00 | 13.108
FLOW WIDTH/DEPTH 3.656Wd m CHRT 32: Vo2/2gDo 0.28 H/Do 0.00 S/Do 2,
Kg side flow 5.08 end flow 4.27 Du/Do 0.83 Qg/Qo 0.63 K 1.73
K vals above for stepped pipes as gate flow $/Do 144 cor 097 Ku 2:39 Kw 230
grate flow decreased by 0.092 from 63/C K vals step pipes as pipe flow Ku 430 Kw 230
5 IN/F IN/F 6 B00 | 40 | 0.000 30 997 0 90 | 26.938) 120 37513) 0.81 | 0.45 Qg 0.090 Qo 0,090 Do 375 0.033 | 100 | 0.146 100 | 0166 | 0.26 | 0.071 | 0.180 | 171 | 11637 | 1.444 | 11590 11590 | 12.850 IN/F
100 to VF 13.00 | 225 | O.1h4 [Pipe flow set by user) (174) CHRT 32: Vo2/2gDo 0.09 H/Do 0.00 Upstregm HGL 11/590 below outlet N36 | 11373
Kg side flow 8.12 end flow 6.20 pipe oby 11.637
Part full downstream pipe Set Kp fo 1
5 VE VE 6 B45 | 138 | 0.000 89 997 0 90 | 13.898) 120 37513) 0.81 | 0.23 Qo 0.090 Do 375 0.033 | 137 | 0.045 164 | 0.054 | 0.26 | 0.037 1.296 | 11328 | 11373 11362 | 13.696 VF
100 to G6/F B45 | 222 | O1hh (Pipe flow= $um upsty atten flpws) (174) CHART 50 Du/Do1.00 alpha 55, 1127 | 11291
K'w 0.26 Vu 0.81 WSE 0.05,
Ku 137 Kw 1.64,
5 G6/F G6/F 66 6.00 190 | 088 | 0.84 | 0.048 | 0.040 | 0.060 | 21 a 0.00 189 | 108.107 | 21 Q GF 368 | 137 | 0.040 | 117 0 6 1M | 6.000 | 120 37513) 1.01 O10 Qg 0.021 Go 0.111 Do 375 0.052 | 194 | 0.101 239 | 0.126 | 0.40 | 0.024 1107 | 11190 | 11.291 NI | 12210 G6/F
100 to GI/F 6.00 303) 0.88 | 100 | 0.048 | 0.048 | 0.048 | 40 3.68 | 220 | 0.192 [Pipe flow=| Sum upstream flows) (174) Angle 44 Chart 39 $/Do 2.5 chartdeg| interp wal for SDo 1.55 Kw 2.39 11.035 | 11166
FLOW WIDTH/DEPTH 0.098Wd m Du/Do 1.00 KO 1.80 K0.5 191 CHART |38
Qu/Qo 0.81 Cg 0.46 K 185 S/Do 2.) KO 1.84|K0.5 1.75/K 1.80
$/Do 2.0 KO 1,98 KO.5 2.10 K 2.04 S/Do 15 KO 2.05 0.5 1.84)K 1,95
$/D0 15 KO 239 KO.5 252K 2.45 Interp yal for S/o 155 Ku 19%
5 GF G/F 66,67 6.00 190 | 0:88 | 0.84 | 0.047 | 0,039 | 0,039 a 62 0.00 189 | 105.107 62 0 B18 36 0.079 | 145 0 d 155 | 8282 | 3.74 375(3)) 1.40 O10 Qg 0.044 Qo 0,155 Do 375 0.100 | 1.51 0.451 151 0151 | 0.78 | 0,064 | 0.178 | 3.00 | 11.015 | 11015 | 11165 1166 | 12.210 G/F
100 to OUT/F 6.00 303] 0.88 100 | 0.047 | 0.067 | 0.047 40 B78 a9 0.239 [Pipe flows $um upste atten flpws) B07) CHART 34 Angle 15 Case 3 10.705 | 10.950
FLOW WIDTH/DEPTH 1.184 Wd m_ $/D025
Du/Do 1.00 Qg/Qo 0.29 K 115.
$/Da 1.40 cor 0.36 Ku 1.51 Kw 151
5 INAH IN/H INAH 6.00 190 | 088 | 0.84 | 0.001 | 0.001 | 0.001 1 1 0.00 88 | 1080.05 1 0 6.00 190 0.001 1 iM | 1224 | 0.50 37513) 1.01 0.02 Qg 0.111 Qo 0.111 Do 375 0.052 | 3.98 | 0.207 3.98 | 0.207 | 0.40 | 0.005 10.381 | 10.888 | 11.095 1095 | 11.265 IN/H
100 te G9/H 6.00 303 | 0.88 100 | 0.001 | 0.001 | 0.001 1 6.00 303 0.001 (Pipe flow set by user) (112) CHRT 32: Vo2/2gDo 0.14 H/Do 135 10.375 | 10.883
FLOW WIDTH/DEPTH 0.00hWd m Kg side flow 3,98 end flow 3.34
5 GOH GOH IN/H,G9 B00 WO | 083 | 0.79 | 0.432 | 0.341 | 0341 | 133 B3 | 0.00 169 | 108.107 | 133 0 GIs! B00 | 0 | 0342 | 271 a a 24 | 6.000 | 050 | 45013} 153 | 0.07 Qg 0.133 Qo 0,244 Do 450 ONS | 171 | 0.206 AN | 0.206 | 0.73 | 0.044 10.430 | 10.679 | 10.883 10.883 | 11112 GOH
100 to G1/] B00 225 | 0.83 | 100 | 0.432 | 0.432 | 0.432 | 270 B00 | 225 | 0.433 [Pipe flow=| Sum upstream flows) (127) CHART 33 Angle 0 10.400 | 10.635
FLOW WIDTH/DRPTH 3.106Wd m $/D0 2.5
Du/Do 0.83 Qg/Qo 0.55 K 149
$/00 2.01 cor 0.22 Ku 171 Kw 1.71
5 GIs! GIO IN/H;G9,610 6.00 190 | 088 | 0.84 | 0.121 | 0.102 | 0102 | 54 5h 0.00 189 | 108.107 | 54 o BOT | 0 | 0404 | 345, 0 4 298 | 5995 | 0.50 | 450(3) 187 | 0.05 Qg 0.054 Qo 0.298 Do 450 0.178 | 0.94 | 0.167 0.94 | 0.167 | 1.09 | 0.066 10.380 | 10.468 | 10.635. 10.635 | 11113 G10!
100 te OUT/G 6.00 303) 0.88 | 100 | 0.421 | 0.121 | 0.4121 | 102 13.07 | 224 | 0554 [Pipe flow=| Sum upstream flows) (127) CHART 33 Angle 2 10.350 | 10.402
FLOW WIDTH/DEPTH 0.880Wd m $/D0 2.5
Du/Do 1.00 Qg/Qo 0.18 K 0.76
‘$/Do 1.57 cor 0.18 Ku 0.94 Kw 0.94
CALCULATIONS TABLE
FILE: N13078-136.dwg DATE: 15-10-2014 TIME: 20:24 OO
Xref's: X-N13078-TIT USR: Curtis Boorman
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