Development Application - Part 2 of 2 - Plans

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

   

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

LOCATION TIME SUB-CATCHMENT RUNOFF INLET DESIGN DRAIN DESIGN HEADLOSSES PART FULU DESIGN LEVELS
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z e i= = <O| tj ljEuluZzl| a} a uw |aal[— o3 oO = nn] unr |odo! = = a So |nol> oatlr Fe 3 — jui-—|—o]rujaco w) ow fo uno = i i = ob] &
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= D> = = a a os) Ze ee . ae Soles a-isa ni S a qo iew|] = <= ojos] So ws o ey a gt Woelrdo > oO o ua Qa ld “ao su 2 |jwajwa}] - co w a e : reat) >
o = < az ZI] Ss jas] = |Sala o}|/>|s jaalsZz\a j2e| 3 ajae/—-S}/-/]e]Ss }sa}/a}]a}]a]a jaslo-|S_ lea fc we 34 a |wowlnat|e a |e alne| & laclaaz}/a | a] > |ao} w]e] wm les] &
w - a 2° zt oa lo = eoo|okw 2 Co > Pr-l2-|loerIz=So = ad = =e Ie = Oo = 2s = - ww -_ —-=|270a/—2i-=z lod co} = Ww ISOojyNwi/tol}aw a Hi-res ir-w srt) w a a: a t >= =
a wn a no a an |Or a =—O}0CO no w nN |no|u~—|eatiSso = we a an |Or|] & - = o = a a a aoa;uw—|rF—-|no n wu oO > |RPOljmP TAC; 4 Tso oO jamjar|)a > o or = 4 = oe no
yrs %_| min |mm/h ha | ha | ha | t/s| l/s} % | I/s I/s | l/s min |mm/h] ha | l/s| l/s} l/s] I/s| im % | mm |m/s|min m m m m m m_|m/s|_m m m m m m
10 | 17a 7H v4 10.09 171/ 0.86] 0.86] 0.070 0.060 0.06 29 | 29 | 0.50] 59 | tocs.1| 29 | 0 2m | 10.09 171 | 0.060] 48 | 694] 19 | 29 | 16.13% 0.40] 37512)0.26| 0.27 Qq 0.029 Qo 0.029 Do 375 0.003] 4.80] 0.017 4.80] 0.017) 0.03] 0.004 2.095] 2.652) 2.669] 2.669) 3.144 17H
100 to 2/4 10.09, 249] 0.86] 1.00] 0.070 0.070 0.074 49 10.09) 249 | 0.070 {Pipe flowt Grate flow) CHRT 32: Vo2/2gD0 0.01 H/Do 2.031) 2.648]
Kg side flow 4.80 end flow 3.65
10 | 2/4 274 17H; 274 10.0 171| 0.86] 0.86] 0.187] 0.16i| 0.161] 76 | 76 | 0.53/ 59 | toos.1] 59 | 17 | 3H | 10.2% 170| 0.221! 176] 717[ 69 | @7 [47.149 0.40] 3751210.79| 0.79 ‘Qg 0.059 Qo 0.087 Do 375 0.032) 1.62| 0.052] 1.85] 0.059 0.25| 0.119 2.011] 2.597| 2.648] 2.655] 2.906  2/H
100 to 3/H 10.09 249] 0.86] 1.00] 0.187) 0.187] 0.187} 129 10.27 247 | 0.257 (Ripe flbw= Sup upstr] atten! tlows)} Angle 49 Chart 39 S/Do 2.5 chart Interp val fpr S/D} 2.72 Kw 1.89 1.822] 2.479]
Du/Do 1.00 KO 1.80 kO.5 1.91 CHART] 38
Qu/Qo 0.33 Cg 1.19 K 1.93 $/Do $.0 KO |! .57 K9.5 1.99 K 1.$9
$/Do 3.0 KO 1.63 KO.5 1.73 K 1.75 $700 2.5 KO |I.70 KO.5 1.66 K 1.65
$/Do 2.5 KO 1.80 KO.5 1.91 K 1.93 Interp val for S/Dp 2.72 Ku 1.6:
10 | 3/4 37H 17H;274; 344 10.0 171| 0.86] 0.86] 0.149] 0.12 0.12 61 | 78 | 0.53] 59 | tocs.1[ 59 | 19 | 47H | 11.08 164] 0.349] 270] 717 | 129 | 141 | 25.52b 0.40] 37512) 1.28] 0.33 Qg 0.057 Qo 0.141 Do 375 0.084 1.26] 0. 105 1.26] 0.105] 0.65] 0.165 1.802] 2.374] 2.479 2.479| 2.622) 3/H
100 to 4/H 10.09 249] 0.86] 1.00] 0.149) 0.149 0.149] 103 11.08 239 | 0.406 (Pipe fibw= Suh upstr] atten! flows)} CHART 33 Angle 0 1700] 2.209]
$/Do 2.5
Du/Do 1.00 Qg/00 0.40 K 1.33
$/Do 2.81 cor -0.07 Ku 1.26 Kw 1.26
10 | 1/K 17K 7K 10.0 171] 0.86] 0.86] 0.208 0.179 0.179 5 | @5 | 0.00] 108 | tocs.i9) @5 | 0 47 | 10.09 171 | 0.179] 144 5 | 12.15% 0.40] 3751)0.77| 0.20 ‘Qq 0.085 Qo 0.085 Do 375 0.030 4.57] 0. 138 4.57] 0.138) 0.24] 0.029 1.749[ 2.238] 2.376| 2.376| 2.615 17K
100 to 4/H 10.00 243] 0.86] 1.00] 0.208 0.208 0.208] 144 10.0 249 | 0.208 (Pipe flows Grate flow) CHRT 32: Vo2/2gDo 0.08 H/Do 1.700] 2.209]
Kg side flow 4.57 end flow 3.61
10 | 4/4 4/4 1783274; 3744 17654 10.0 171] 0.86] 0.86] 0.056 0.049 0.048, 23 | 42 | 0.53] 59 | 1os.1] 42 | 0 5/4 | 11.39 162 | 0.576] 441 | 717 | 182 | 260 | 32.04% 0.40] 5251¢)1.16| 0.46 Qg 0.040 Qo 0.260 Do 525 0.069| 0.95] 0.065 0.95| 0.065] 0.33] 0.107] 1.830] 2.144[ 2.209 2.209] 2.468 4/H
100 to 5/H a 10.00, 249] 0.86] 1.00] 0.056 0.056 0.056) 39 11.39 237 | 0.670 [Fipe fipw= Sum upstr| at ten| flows) Routine 2.2 17K até 3/H 1.702] 2.037|
CHART 48 Vel! |.261 Vel2 0.729
Du/Do 0.71 Qu/Qo 0.54 K 0.85 Eq Dig 512 Angle 1$3 Flow 0.220
4/00 2.0 chrt Qg/Qo 0.15 Kg 0.13 CHART] 33 Angie 0
4/Do 1.5 chrt Qg/Qo 0.15 Kg 0.14 S/o 2.5
4/0 1.60 Interp value Kg 0.14 Du/Do|0.98 dg/do 0} 15 K d.66
Kuskw: 0.99 $/D0 }.70 cor 0.13|Ku 0.78 Kw 0/79
Combined pipes in line case Interpolated Ku= 0/95 Kws| 0.95
Join Pipes:
10 | 5/4 S/H 17K:4 10.009, 171/ 0.86] 0.86] 0.070 0.06q 0.060 29 | 29 | 0.50] 59 | tocs.1] 29 | © eH | 11.89 160 | 0.636] 479 | 694] 195 | 264 | 11.69) 0.40] 52512) 1.27 0.15 Qg 0.027 Qo 0.284 Do 525 0.082) 1.68] 0.139) 2.04| 0. 168 0.40] 0.046 1.682] 1.898 2.037 2.066] 2.325  5/H
100 to 6/H 10.00, 243] 0.86] 1.00] 0.070 0.074 0.079 48 11.89 233 | 0.740 \Fipe fipw: Sum upstr] at ten| lows) Angle 12 Chart 36 S/Do 2.5 chart Interp val thr S/D} 1.73 kw 2.04 1.635] 1.852]
Du/Do 1.00 KO 1.5! KO.5 1.86 chart] 35
Qu/Qo 0.90 Cg 0.24 K 1.59 $/D0 2.0 KO |I.55 K9.5 1.74 K 1.99
$/Do 2.0 KO 1.79 KO.5 2.07 K 1.86 s/00 |.5 KO |I.75 KO.5 1.80 K 1.{6
$/Do 1.5 KO 2.11 KO.5 2.54 K 2.21 Interp val fpr S/D} 1.73 ku 1.6
10 | 6/H 6/H 17H; 27H; 3/04 17K;4 10.0] 17i] 9.88/ (0.08] 0. 69] 0.142 0.149 o7 | er | 0.80] 99 | 1oss.1/ 89 | 8 o | 12.09 159] 0.77] 503 | 694 | 247 | 337 | 22.54% 0.40] 5251%)1.50| 0.25 Qq 0.055 Qo 0.337 Do 525 0.115, 1.75] 0.201 2.24] 0.257) 0.56] 0.126] 1.615] 1.651] 1.852 1.908] 2.142] 6/H
100 to 7/H 7H:5/H;6/ 10.00, 249] 0.86] 1.00| 0.165 0.165 0.165) 114 12.09 232 | 0.905 (Hipe fipws Sum upstr] at ten| flows) Angle 12 Chart 36 S/Do 2.5 chart Inter val fr S/Dp 1.56 Kw 2.2 1.525] 1.525
Du/Do 1.00 KO 1.51 KO.5 1.86 CHART] 35
Qu/Qo 0.84 Cq 0.40 K 1.65 $/Do 2.0 KO |I.55 K9.5 1.74 K 1.52
$/Do 2.0 KO 1.79 KO.5 2.07 K 1.90 /Do | -5 KO |I.75 KO.5 1.80 K 1.77
$/Do 1.5 KO 2.11 KO.5 2.54 K 2.28 Interp val for S/Dp 1.56 ku 1.7!
10 | 170 170 7) 10.09 171| 0.86] 0.86] 0.162 0.139 0.139] 66 | 66 | 0.50] 122] 12cs.3] 66 | o 270 | 10.09 171 | 0.139] 112] 694] 46 | 66 | 13.612 0.40] 3751%)0.60| 0.23 Qg 0.066 Qo 0.066 Do 375 0.018 4.41 | 0.081 4.41| 0.081] 0.14] 0.019 2.220| 2.785] 2.866 2.866] 3.437, 1/0
100 to 2/0 10.09 249] 0.86] 1.00] 0.162 0.162 0.162 112 10.09 249 | 0.162 {Pipe flowt Grate flow) CHRT 32: Vo2/2gDo 0.05 H/Do 2.166] 2.766
Kg side flow 4.41 end flow 3.49
10 | 2/0 2/0 170;2/D 10.0 171] 0.86] 0.86] 0.169] 0.149 0.144 69 | 69 | 0.50] 59 | 1ocs.1] 59 | 10 | 37D | 10.23 170] 0.285] 227 | 694| 103 | 124 | 20.474 0.50| 3751%)1.13| 0.30 Qg 0.059 Qo 0.124 Do 375 0.065] 1.55] 0.101 1.55] 0.101] 0.50] 0.103 2.146] 2.665] 2.766| 2.766| 2.982 2/0
100 to 3/0 10.09 249] 0.86] 1.00] 0.169] 0.169 0.169 117 10.23] 247 | 0.331 (Hipe fipws Sup upstr| at ten| flows) CHART 34 Angle 25 Case 3 2.043] 2.562|
$/D0 2.5
Du/Do 1.00 Qg/00 0.47 K 1.60
$/D0 2.65 cor -0.05 Ku 1.55 kw 1.56
10 | 3/0 3/0 170;270;3}0 10.0 171| 0.86] 0.86] 0.044] 0.03e 0.038] 18 | 28 | 0.50/ 59 | Jocs.1] 28 | o 4/0 | 10.53 168 | 0.323[ 254 | 694] 104] 150 | 8.ea5| 0.40/ 4501%)0.95| 0.15 ‘Qg 0.028 Qo 0.150 Do 450 0.046 1.54] 0.071 1.75] 0.080 0.28] 0.025 2.098| 2.491] 2.562| 2.571| 2.934 3/0
100 to 4/0 10.0 249] 0.86 1.00] 0.044 0.044 0.044 31 10.53, 244 | 0.375 (fipe flbws Sum upstr| af ten| flows) Angle 15 Chart 36 S/Do 2.5 chart Interp val fpr S/D} 2.05 kw 1.7: 2.062) 2.466]
Du/Do 0.83 KO 1.37 KO.5 1.80 CHART] 35
Qu/Qo 0.82 Cq 0.44 K 1.56 S/o 2.5 KO |1.25 K).5 1.65 K 1.43
$/D0 2.5 KO 1.37 KO.5 1.80 K 1.56 $/00 2.0 KO |!.45 K9.5 1.60 K 1.
$/D0 2.0 KO 1.59 KO.5 2.00 K 1.77 Interp val fr S/0} 2.05 ku 1.54
io | 470 470 170;2/0;3/0;;4/0 10.09 171] 0.86] 0.86] 0.140 0.120 0.120 57 | 57 | 0.50/ 59 | toos.1] 57 | 0 176 | 10.68 167 | 0.443| 34a | 694[ 143 | 205 | 12.82] 0.40/ 5251#10.92| 0.21 Qg 0.056 Qo 0.205 Do 525 0.043] 1.68] 0.072) 1.91] 0.084 0.21] 0.027] 2.117| 2.394] 2.466 2.476| 2.702] 4/0
100 to 5/D 10.00 243] 0.86] 1.00] 0.140 0.140 0.140 97 10.68 243 | 0.515 (Ripe fipw= Sum upstr| at ten| lows) Angle ST Chart 43 $/Do 2.5 chart Interp val fr S/Dp 1.68 Kw 1.9 2.066| 2.367
Du/Do 0.86 KO 1.35 KO.5 cHart] 42
Qu/de 0:73 Cy 0.62 Kiv62. $/D0 2.0 KO |I.10 K9.5 1.94 K 1.63
$/0 2.0 KO 1.41 KO.5 1.98 K 1.77 s/o |-5 KO |I.15 k9.5 2.06 K 1.71
$/D0 1.5 KO 1.61 KO.5 2.21 K 1.99 Interp val fr S/D) 1.68 ku 1.68
io | WF VE VF 10.0 171] 0.86] 0.86] 0.072 0.062 0.062 29 | 29 | 0.50/ 35 | i2es.1] 29 | 0 176 | 10.09 171 | 0.062] 50 | 694] 21 | 29 | 9.355 0.40] 37512)0.26| 0.16 Qg 0.029 Qo 0.029 Do 375 0.003) 6.01 | 0.021 6.01] 0.021] 0.03] 0.003) 1.954] 2.370 2.390 2.390| 3.011] 17F
100 to 5/D 10.09 249] 0.86] 1.00] 0.074 0.074 0.072] 50 10.0 249 | 0.072 (Pipe flowt Gratel flow) CHRT 32: Vo2/2gDo 0.01 H/Do 1.916] 2.367]
Kg side flow 6.01 end flow 4.40
10 | 5/0 5/D 170;2/0;3/044/0; 1 16 10.89 166 | 0.505] 393 694] 161 | 232 | 65.237 0.40] 52512)1.04| 1.05 Qo 0.232 Do 525 0.055 2.39] 0.132] 2.39] 0.139 0.27| 0.174 2.046| 2.236] 2.367] 2.367| 2.771] 5/0
100 to 6a/D ne 10.89 241 | 0.587 [Ripe fipw= Sup upstr| at ten| tlows)| Routine 2.3 Low vel late I/F 1.785} 2.062]
CHART 49 Div 375 Olv ).028 Biv/Do p.71
High vel tat 4/0 Qiv/oy 0.12 L 0.05]H-L 2.69
Dhy 525 Qhy 0.204 No gr¢te flow: H-L10.2 = 2.39
Dhv/Div 1.4 Dhv/Do 1.00 KusKwt 2.39
Qhv/Qo 0.88 H 2.64
io | 176 176 176 10.0 171] 0.86] 0.86] 0.125 0.107 0.1071 51 | 51 | 0.00] 108 | toes.1 51 | 0 6/0 | 10.0 171 | 0.107/ 86 51 | 7.256 0.40] 375(2)0.46] 0.12 9 0.051 Qo 0.051 Do 375 0.011! 5.80] 0.063 5.80] 0.063) 0.08] 0.004 1.664] 2.068| 2.131 2.131] 2.46 176
100 to 60/D 10.00 249] 0.86] 1.00] 0.125 0.125 0.125 86 10.0 249 | 0.125 (Pipe flows Gratel flow) CHRT 32: Vo2/2gDo 0.03 H/Do 1.635] 2.062
Kg side flow 5.80 end flow 4.33
10 | 6a/D 60/D 170;2/0;3/04470; 1 16 11.94 159 | 0.612] 459 270 | 18.48] 0.40] 52512)1.20] 0.26 Qo 0.270 Do 828 0.073! 0.72| 0.053 0.73] 0.054 0.36] 0.066 1.765] 2.003] 2.062 2.063] 2.347] 60/0
100 to 6/D FF A/G 11.94 232 | 0.712 (Ripe fipw= Sum upstr| atten! lows) Eq Di 610 Angle 189 Flow 0.270 1691] 1.943]
es in line case CHART] 50 Du/Do! . 16] a1 pha Db
Kw 0105 Vu .92 W5E 0.04
1/6 and 5/D Ku 0.75 Kw 0.78
Vell 1.027 Vel2 0.429 Interpolated Kuz 0|72 Kws 0.73
10 | 6/0 6/0 170;2/D;3/044/0; | 10.0 171] 0.86] 0.86] 0.241] 0.208 0.208 99 | 99 | 0.50] 59 | tocs.1! 59 | 40 | 7/0 | 12.2 158 | 0.820] 609| 694 | 286 | 322 | 9.073) 0.40| 52512)1.44] 0.11 Qg 0.055 Qo 0.322 Do 525 0.106 0.90] 0.095] 0.90] 0.038) 0.51| 0.047] 1.671] 1.848] 1.943 1.943] 2.384 6/0
100 to 77D FF 1/66 10.00 249] 0.86] 1.00] 0.241] 0.241] 0.241] 167 12.29 230 | 0.953 (Ripe fipw= Sup upstr| at ten| tlows)| CHART 33 Angle 5 1.635] 1-801
$/D0 2.5
Du/Do 1.00 Q9/00 0.17 K 0.72
$/Do 1.52 cor 0.18 Ku 0.90 Kw 0.90
io | 7 7 170;2/0;3/D44/0; 1 10.0 171| 0.86] 0.86] 0.102] 0.088 0.08] 42 | 82 | 0.50] 59 | tocs.1] 59 | 23 o | 12.3i] 157 | 0.908] 671 | 694 | 297 | 375 | 22.499 0.40] 52514) 1.67] 0.22 Qg 0.054 Qo 0.375 Do 525 0.142) 0.84 0.119 0.84/ 0.119 0.69] 0.156 1.615] 1.681] 1.801 ¥.e01 2.153) 77D
100 to 8/0 | /F;1/6;6/047/0 10.0 249] 0.86] 1.00] 0.102 0.102) 0.103 71 12.31] 229 | 1.055 (Pipe fipw= Sum upstr] atten! flows) CHART 33 Angle 4 1.525] 1.525]
$/D0 2.5
Du/Do 1.00 Q9/00 0.14 K 0.65
$/Do 1.35 cor 0.19 Ku 0.84 Kw 0.84
( Y Ye “y > >
aa Consulting Engineers N sheet 1 of2 sheets
Seems pee nears e NOOSA DOMAIN RETIREMENT VILLAGE |_—
‘SUNSHINE COAST ‘GLADSTONE Gs Joo NoT SCALE FROM THIS DRAWING - USE ONLY DIMENSIONS PROVIDED -IFINDOUBT PLEASE ENaUIRE J atum: — AHD derived cain CH drawing number
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telephone (07) 5443 2500 telephone (07) 4072 2100
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