7.schematic Diagram Model
7.schematic Diagram Model
7.schematic Diagram Model
Q=0.0317 cumecs;
FRL = 454.663 m FRL = 472.378 m FRL = 587.426 m FRL = 582.598 m FRL = 523.673 m
HGL = 470.22m TC = 4.75 MCFT HGL = 637.83 m HGL = 636.81 m HGL = 625.10m
HGL = 477.76 m HGL = 650.60 m HGL = 625.48 m HGL = 621.85 m
RH = 0.2 mwc FRL = 418.125 m RH = 43.3 mwc RH = 54.2 mwc RH = 31.6 mwc
RH = 23.1 mwc RH = 178.2 mwc RH = 38.1 mwc RH = 98.2 mwc
RAMASAMUDRAM TANK (5)
DI PIPE
TC = 16.50 MCFT JANGAMAKERI TANK (7)
FRL = 416.44 m TC = 12.71 MCFT
HGL = 490.96m FRL = 518.717 m
L=5097 m; V=0.63m/sec
VT PUMPS DI PIPE
Q=0.1006 cumecs;
Q=0.0506 cumecs;
Q=0.0699 cumecs;
Q=0.0104 cumecs;
Q=0.0211 cumecs;
Q=0.0547 cumecs;
Q=0.0255 cumecs;
Q=0.0087 cumecs;
VT-6&7 : 0.7144 Cumecs 2 (1W+1S) Q=0.0925 cumecs;
Q=0.06 cumecs;
(2572 Cum/hr ; 202 mwc )
Q=0.1242 cumecs;
L=4664m; V=0.68 m/sec
MAXIMUM WATER LEVEL = 457 m Pipe ID=416.4 mm; t=6.3 mm
MINIMUM WATER LEVEL = 456 m H Loss=5.78 m; D/t =82
MS PIPE
MS PIPE
MS PIPE
MS PIPE
DI PIPE
DI PIPE
DI PIPE
DI PIPE
FULL SUPPLY LEVEL = 642 m
DI PIPE
MS PIPE
STATIC HEAD = 186 m
G PIPE LINE LOSS =13.67 m
RISING MAIN G
RM-2
HGL= 655.67
SRM-2 PH-2
SRM-4 GRAVITY MAIN GM-1 GM-4
MS PIPE HGL=484.01 MS PIPE MS PIPE HGL=457.15 MS PIPE MS PIPE MS PIPE MS PIPE MS PIPE HGL=639.83 MS PIPE DI PIPE DI PIPE GM-7
MS PIPE
DC-1 HGL=634.15
Q=0.9042 cumecs; Q=0.8333 cumecs; Q=0.7634 cumecs; Q=0.7144 cumecs; Q=0.7144 cumecs; Q=0.6138 cumecs; Q=0.0305 cumecs;
SRM-1 SRM-3 L=2190m; V=1.42 m/sec
SRM-5 Q=0.4896 cumecs; GM-2 Q=0.4792 cumecs; GM-3 Q=0.4581 cumecs; Q=0.1107 cumecs; GM-5 Q=0.056 cumecs; GM-6
L=3980m; V=1.42 m/sec L=5700m; V=1.31 m/sec L=6700m; V=1.52 m/sec L=60m; V=1.42 m/sec L=5080 m; V=1.22 m/sec L=1160m; V=0.77 m/sec HGL=641.26 L=790m; V=0.75 m/sec HGL=640.77 L=1660m; V=0.72 m/sec L=1450 m; V=0.56 m/sec HGL=638.79 L=1580 m; V=0.72 m/sec HGL=635.77 L=1092 m; V=0.56 m/sec
HGL=491.88 Pipe ID=900 mm; t=7 mm Pipe ID=900 mm; t=7 mm HGL=474.33 Pipe ID=800 mm; t=6.5 mm Pipe ID=800 mm; t=6.5 mm Pipe ID=800 mm; t=9 mm HGL=650.69 Pipe ID=800 mm; t=8 mm DELIVERY CHAMBER DC-1 Pipe ID=900 mm; t=6 mm Pipe ID=900 mm; t=6 mm Pipe ID=900 mm; t=6 mm Pipe ID=500 mm; t=5 mm Pipe ID=314.8 mm; t=5.6 mm Pipe ID=263.4 mm; t=5.3 mm
Q=0.0218 cumecs;
Pipe ID=211.1 mm; t=4 mm
Q=0.9642 cumecs;
Q=0.0203 cumecs;
Q=0.3474 cumecs;
Q=0.049 cumecs;
DI PIPE
KESAWAR TANK (15A)
TC = 80.48 MCFT
MS PIPE
MS PIPE
MS PIPE
MS PIPE
TC = 28 MCFT
FRL = 599.363 m
HGL = 634.23 m GURAMITKAL TANK (14)
RH = 34.9 mwc MS PIPE DI PIPE TC = 19.07 MCFT
JACK WELL CUM
PUMP HOUSE PH-1 Q=0.3058 cumecs; GM4-R1 Q=0.0416 cumecs; FRL = 607.487 m
F HGL = 638.23 m F
VT PUMPS L=4475 m; V=0.80m/sec HGL=638.27 L=30 m; V=0.53 m/sec
VT-1,2 : 0.9642 Cumecs 2 (1W+1S) MINASAPURA NAZARAPUR Pipe ID=700 mm; t=5 mm Pipe ID=314.8 mm; t=5.6 mm RH = 30.7 mwc
BURAGAPALLI TANK /
(3472 Cum/hr ; 177 mwc ) TANK (15C) TANK (15B) H Loss=4.04 m; D/t =142 H Loss=0.04 m; D/t =62 ITAKAL TANK (12)
MAX. WATER LEVEL = 363.158 m ANAPUR TANK (18) TC =16.4 MCFT TC =10.00 MCFT
RH = 52.5 mwc TC = 28 MCFT TC =25.70 MCFT
MINIMUM WATER LEVEL = 355 m FRL = 440.023 m FRL=604.521 m
HGL = 478.03 m FRL = 599.363 m FRL = 469.219 m
FULL SUPPLY LEVEL = 457 m
FRL = 425.563 m GM-14 HGL=631.38 m
STATIC HEAD = 102 m HGL = 447.86m GORANUR TANK (20)
TC = 9.30 MCFT HGL=409.94 RH = 26.9 mwc
PIPE LINE LOSS =72.85 m
GOPALAPUR TANK (4) RH = 6.2 mwc DI PIPE DI PIPE TC = 16.00 MCFT
HGL = 529.85 m FRL = 389.717 m
PH-1 Q=0.0196cumecs; Q=0.0349 cumecs;
HGL =406.78m
L=3330m; V=0.56 m/sec L=1665m; V=0.64 m/sec
BHIMA RIVER
NASALWAYI TANK (19) Pipe ID=212 mm; t=5 mm Pipe ID=263.4mm; t=5.3 mm RH = 17.1mwc
TC = 9.00 MCFT
Q=0.0545 cumecs;
PUMP HOUSE PH-1 RH = 4.9 mwc
TC = 5.3 MCFT TC = 2.84 MCFT
INTAKE POINT LEVEL = 344 m
VT PUMPS
VT-3,4,5: 1.7441 Cumecs 3 (2W+1S) FRL = 367.557 m FRL = 390.000 m KALABELAGUNDI GOAN
(3140 Cum/hr ; 152 mwc ) KARANAGI TANK (21)
MAX. WATER LEVEL = 363.158 m TANK (26)
DI PIPE
MINIMUM WATER LEVEL = 355 m TC = 4.00 MCFT
TC = 3.48 MCFT
FULL SUPPLY LEVEL = 417 m FRL = 390.433 m
FRL = 406.763 m
HGL = 412.39m
INTAKE CANAL
GM-13
HGL = 503.83 m
FRL = 388.918 m FRL = 408.412 m YELASATTI TANK (23)
Pipe ID=1100 mm; t=8.5mm
FRL = 402.592 m
RH = 76.0 mwc RH = 48.1 mwc Q=0.013 cumecs;
Q=0.0288 cumecs;
Q=0.0076 cumecs;
Q=0.0675 cumecs;
Q=0.0087 cumecs;
MS PIPE
TC =20.00 MCFT
DI PIPE
GI PIPE
DI PIPE
RISING MAIN RM-3
FRL=380.60 m
Q=0.7846 cumecs; HGL=410.76 m
L=2230 m; V=1.56m/sec DELIVERY CHAMBER DC-3 RH = 30.2 mwc YIDALUR TANK (22A)
SRM-6 SRM-9 RISING MAIN RM-3 SRM-11 Pipe ID=800 mm; t=6 mm SRM-12 FULL SUPPLY LEVEL = 417 m GM-15 TC =4.04 MCFT
HGL=494.52 MS PIPE MS PIPE MS PIPE HGL=448.12 MS PIPE MS PIPE HGL=439.08 MS PIPE H Loss=6.02 m; D/t =135.3 HGL=433.06 MS PIPE MS PIPE HGL=416.98 DI PIPE DI PIPE FRL=380.019 m
DC-3
Q=1.7297 cumecs; SRM -7 Q=1.709 cumecs; SRM -8 Q=1.6802 cumecs; Q=1.6431 cumecs; SRM -10 Q=1.6355 cumecs; Q=0.8509cumecs; Q=0.7178 cumecs; Q=0.6503 cumecs; Q=0.0815 cumecs; GM-16 Q=0.0728 cumecs;
L=11560 m; V=1.82 m/sec HGL=465.95 L=2180 m; V=1.80 m/sec HGL=460.68 L=5360 m; V=1.77 m/sec L=2190 m; V=1.73 m/sec HGL=443.19 L=1840 m; V=1.72 m/sec L=30 m; V=1.69 m/sec L=3700 m; V=1.87m/sec L=20 m; V=0.68 m/sec L=4050 m; V=0.60 m/sec HGL=413.02 L=2830 m; V=0.54 m/sec
Pipe ID=154.3mm; t=4.8 mm
Pipe ID=1100 mm; t=8.5mm Pipe ID=1100 mm; t=8mm Pipe ID=416.4 mm; t=6.3 mm Pipe ID=416.4 mm; t=6.3 mm
H Loss=28.57m; D/t =131.4 H Loss=5.27 m; D/t =131.4 H Loss=12.56 m; D/t =139.5 H Loss=4.93 m; D/t =139.5 H Loss=4.11 m; D/t =139.5 H Loss=0.10m ; D/t =135.3 H Loss=16.22 m; D/t =118.6 H Loss=0.02 m; D/t =159.1 H Loss=3.96 m; D/t =82 H Loss=2.26m; D/t =82
L=9080m; V=0.77 m/sec
D D
Q=0.0668 cumecs;
TC = 6.80 MCFT DELIVERY CHAMBER DC-2
Q=0.5688cumecs;
Q=0.0144cumecs;
Q=0.0371cumecs;
RH = 9.6 mwc
MS PIPE
MS PIPE
DI PIPE HGL=402.24 MS PIPE
GI PIPE
Q=0.6592cumecs;
Q=0.0148 cumecs;
MS PIPE
Q=0.1917 cumecs;
L=1075m; V=0.74m/sec L=4650 m; V=0.68m/sec
Pipe ID=160 mm; t=5mm Pipe ID=600 mm; t=5mm GUDALGUNTA TANK (31)
HGL=404.22
FRL=361.611 m FRL=393.663 m HGL = 402.30 m TC =18.36 MCFT FRL=397.181 m
DI PIPE RH = 10.0 mwc
GM-9
HGL=449.46 m HGL=439.08 m HGL=416.94 m
0.1769 cumecs;
FRL=406.422 m
RH = 87.8 mwc RH = 45.4 mwc RH = 19.8 mwc
Q=0.0124cumecs; HGL=432.27 m
KANEKAL SMALL TANK L=605m; V=0.62 m/sec RH = 25.8mwc
MS PIPE
KILANKERI TANK (27A) (29A) Pipe ID=160 mm; t=5 mm WAKSAMBRA TANK (25A) WADAWAT TANK (24A)
TC =8.28 MCFT H Loss=1.92 m; D/t =34.1 TC =9.00 MCFT TC =8.28 MCFT
TC = 10.00 MCFT
FRL=380.123 m FRL=384.049 m FRL=380.123 m
FRL = 380.197 m
GRAVITY MAIN
KILANKERI TANK (27B) TC = 14.80 MCFT TC =24.30 MCFT AZALPUR TANK (24B)
Q=0.6468cumecs;
TC =15.40 MCFT FRL = 371.580m FRL=384.215 m TC =15.40 MCFT
GM-2
FRL=372.137 m HGL=401.78 m FRL=372.137 m
RH = 17.6 mwc
MS PIPE
BADDEPALLI THOOR
TANK (30A)
TC = 13.40 MCFT SAMBRA TANK (30)
FRL = 376.421 m TC = 53.00 MCFT
BADDEPALLI DUBBAL FRL = 386.447 m
TANK NAME
HGL=403.96
TANK (30B) HGL = 403.93 m
GM-10
TANK NUMBER RH = 17.5 mwc MS PIPE
TC = 13.40 MCFT
FRL = 376.421m Q=0.386 cumecs;
LINGERI TANK (1) L=20m; V=0.77 m/sec
Pipe ID=800 mm; t=6mm
FRL = 361.611 m H Loss=0.03m; D/t =135.3
RH = 24.9 mwc
HYDRAULIC GRADIENT LINE
B RESIDUAL HEAD AT TANK KADECHUR SOMA DEVI B
MS PIPE
TANK (32A)
ABBREVIATIONS FOR TANK DETAILS TC = 6.18 MCFT SWARASTRAHALLI TANK (32)
FRL = 368.138 m TC = 16.74 MCFT
FRL = 373.943 m
HGL = 396.49
LEGEND RH = 22.5 mwc
DI PIPE
INTAKE CANAL / FOREBAY Q=0.0609 cumecs;
L=845m; V=0.78 m/sec
FLOW DISCHARGE RISING MAIN Pipe ID=314.8 mm; t=5.6mm
H Loss=1.89 m; D/t =64.7
Pipe ID =600mm; t=5mm;
VELOCITY
LENGTH OF PIPE GRAVITY MAIN
Q=1.7297 cumecs;
Q=0.1999cumecs;
BUTTERFLY VALVE
L=11560 m; V=1.82m/sec
JACKWELL/PUMPHOSE
Pipe ID=1100 mm; t=8.5mm JOB No. : LE180239 TITLE :
MS PIPE
FRICTION LOSS +
FITTING LOSS D/t Ratio KADECHUR ERAMMA TANK (33) DUPPALLI TANK (34) SCHEMATIC LINE DIAGRAM
A TC = 15.60 MCFT TC = 75.95 MCFT A
ABBREVIATIONS FOR PIPE LINE DETAILS FRL = 368.696 m DI PIPE MS PIPE FRL = 365.028 m NOTES:
HGL = 394.83 m HGL = 394.51 m 1. THE SCHEMATIC DIAGRAM SHOWS BRIEFLY THE PIPE LINE FLOW & TANK FILLINGS.
Q=0.034cumecs; Q=0.1659 cumecs; RH = 29.5 mwc
RH = 26.1 mwc L=455m; V=0.62 m/sec GM-12 L=1848m; V=0.59 m/sec 2. PIPE LINE MENTIONED ABOVE ARE APPROXIMATE VALUE.
Pipe ID=263.4mm; t=5.3mm HGL=395.66 Pipe ID=600mm; t=5mm 3. THIS DRAWING SHALL BE READ IN CONJUNCTION WITH INDEX MAP.
H Loss=0.83m; D/t =54.6 H Loss=1.15m; D/t =122
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