Line Size - Enereco
7
LINE SIZE SHEET By A-M Job N˚ Date Rev: Line N˚ Line Descrption Section 1: From Drainage to Intercetor Pit Fluid in line Water Liquid flow (l/min) 5052.0 GPM (des.) 1334.59 Temperature 140 ˚ F Recommended Velocity . 7.0 ft/sec 2.1336 m/sec Sp. Gr 1.00 Inside Diameter 8.82 in 224.0211 mm Viscosity 0.46 Cp Inside Diameter Choosen 9.75 in 247.65 mm Actual velocity 5.73 ft/sec 1.745879 m/sec Reynolds number 9.38E+05 Turbulent ξ/D 0.000021 f 0.0124 0.0130 Pressure Drop per 1 feet of pipe 0.0034 Psia 0.00023 bara Suction elevation Head 0.69 ft 0.21 m Hydrostatic pressure 0.298 Psi 0.02055 bara Total length 82.02 ft 25 m ∆P in straight pipe 0.2762 Psia 0.01905 bara Fittings,valves expansion, contraction, etc Equipment Item Number of item k Item ∆P psia Ball Valve 0 0 Gate Valve 0 0 0 0.00 Strainer 0 0 0.00 Sharp Edged Exit 0 0.00 Tee 0 0.00 Others 0 Sudden Contraction 0 0.00000 Total 0 Total 0 ∆P through valves and fittings 0.0000 Psia 0.000 bara ∆P through line 0.2762 Psia 0.019046 bara Total pressure Drop 0.022 Psia 0.002 bara Section 1: From Intercetor Pit to Evaporation Pond Fluid in line Water Liquid flow (l/min) 5052.0 GPM (des.) 1334.59 Temperature 140 ˚ F Recommended Velocity . 7.0 ft/sec 2.1336 m/sec Sp. Gr 1.00 Inside Diameter 8.82 in 224.0211 mm Viscosity 0.46 Cp Inside Diameter Choosen 9.75 in 247.65 mm Actual velocity 5.73 ft/sec 1.745879 m/sec Reynolds number 9.38E+05 Turbulent ξ/D 0.000021 f 0.0122 0.0130 Pressure Drop per 1 feet of pipe 0.0033 Psia 0.00023 bara Suction elevation Head 2.74 ft 0.84 m Hydrostatic pressure 1.185 Psi 0.08172 bara Total length 331.36 ft 101 m ∆P in straight pipe 1.0977 Psia 0.07571 bara Fittings,valves expansion, contraction, etc Equipment Item Number of item k Item ∆P psia Ball Valve 0 0 Gate Valve 0 0 0 0.00 Strainer 0 0 0.00 Sharp Edged Exit 0 0.00 Tee 0 0.00 Others 0 Sudden Contraction 0 0.00000 Total 0 Total 0 ∆P through valves and fittings 0.0000 Psia 0.000 bara ∆P through line 1.0977 Psia 0.075706 bara Total pressure Drop 0.087 Psia 0.006 bara ft 90˚ Elbow 45˚ Elbow ft 90˚ Elbow 45˚ Elbow
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Transcript of Line Size - Enereco
LINE SIZE SHEETBy A-M Job N˚
Date Rev:
Line N˚
Line Descrption
Section 1: From Drainage to Intercetor Pit
Fluid in line Water
Liquid flow (l/min) 5052.0 GPM (des.) 1334.59 Temperature 140 ˚ F 60 ˚ C
Recommended Velocity . 7.0 ft/sec 2.1336 m/sec Sp. Gr 1.00
Inside Diameter 8.82 in 224.02107 mm Viscosity 0.46 Cp
Inside Diameter Choosen 9.75 in 247.65 mm
Actual velocity 5.73 ft/sec 1.7458788 m/sec
Reynolds number 9.38E+05 Turbulent
ξ/D 0.000021
f 0.0124
0.0130
Pressure Drop per 1 feet of pipe 0.0034 Psia 0.00023 bara
Suction elevation Head 0.69 ft 0.21 m
Hydrostatic pressure 0.298 Psi 0.02055 bara
Total length 82.02 ft 25 m
∆P in straight pipe 0.2762 Psia 0.01905 bara
Fittings,valves expansion, contraction, etc Equipment
Item Number of item k Item ∆P psia
Ball Valve 0 0
Gate Valve 0 0
0 0.00 Strainer 0
0 0.00
Sharp Edged Exit 0 0.00
Tee 0 0.00 Others 0
Sudden Contraction 0 0.00000
Total 0 Total 0
∆P through valves and fittings 0.0000 Psia 0.000 bara
∆P through line 0.2762 Psia 0.0190463 bara
Total pressure Drop 0.022 Psia 0.002 bara
Section 1: From Intercetor Pit to Evaporation Pond
Fluid in line Water
Liquid flow (l/min) 5052.0 GPM (des.) 1334.59 Temperature 140 ˚ F 60 ˚ C
Recommended Velocity . 7.0 ft/sec 2.1336 m/sec Sp. Gr 1.00
Inside Diameter 8.82 in 224.02107 mm Viscosity 0.46 Cp
Inside Diameter Choosen 9.75 in 247.65 mm
Actual velocity 5.73 ft/sec 1.7458788 m/sec
Reynolds number 9.38E+05 Turbulent
ξ/D 0.000021
f 0.0122
0.0130
Pressure Drop per 1 feet of pipe 0.0033 Psia 0.00023 bara
Suction elevation Head 2.74 ft 0.84 m
Hydrostatic pressure 1.185 Psi 0.08172 bara
Total length 331.36 ft 101 m
∆P in straight pipe 1.0977 Psia 0.07571 bara
Fittings,valves expansion, contraction, etc Equipment
Item Number of item k Item ∆P psia
Ball Valve 0 0
Gate Valve 0 0
0 0.00 Strainer 0
0 0.00
Sharp Edged Exit 0 0.00
Tee 0 0.00 Others 0
Sudden Contraction 0 0.00000
Total 0 Total 0
∆P through valves and fittings 0.0000 Psia 0.000 bara
∆P through line 1.0977 Psia 0.0757061 bara
Total pressure Drop 0.087 Psia 0.006 bara
ft
90˚ Elbow
45˚ Elbow
ft
90˚ Elbow
45˚ Elbow
B16
figure 2-11 page 68 LUDWIG
B49
figure 2-11 page 68 LUDWIG
LINE SIZE SHEETBy A-M Job N˚Date 4/7/2023 23:55 Charge N˚Line N˚Line Descrption
Pump suction
Fluid in line TEG Temperature 140 ˚ FGPM (Calc.) 1100.717 GPM (des.) 1100.717 Source Pressure 200.1521 psiaRecommended Velocity . 4.0 ft/sec Sp. Gr 0.49Inside Diameter 10.60 in Viscosity 0.4 CpInside Diameter Choosen 11.938 in Liquid Vapor Pressure 200.1521 psiaActual velocity 3.15 ft/secReynolds number 3.53E+05 Turbulentξ/D 0.000151f 0.0150
0.0130Pressure Drop per 1 feet of pipe 0.0005 PsiaSuction elevation Head 73.82 ftHydrostatic pressure 4.13 PsiaTotal length 45.20 ft∆P in straight pipe 0.5000 PsiaFittings,valves expansion, contraction, etc EquipmentItem Number of item k Item ∆P psiaBall Valve 0 0
0 0.00 Strainer 0Sharp Edged Entrance 0 0.00Sharp Edged Exit 0 0.00Tee 0 0.00 Others 0Total 0 Total 0
∆P through valves and fittings 0.2000 Psia∆P through line 0.7000 PsiaSuction pressure 203.582 Psia
ft
90˚ Elbow
B16
figure 2-11 page 68 LUDWIG
NPSH Available 70.485 ft 21.48379
Discharge suction
Temperature 140 ˚ FGPM (Calc.) 1100.717 GPM (des.) 1100.717 End Pressure 365.4 psiaRecommended Velocity . 8.0 ft/sec Sp. Gr 0.49Inside Diameter 7.49 in Viscosity 0.4 CpInside Diameter Choosen 7.981 inActual velocity 7.05 ft/secReynolds number 5.28E+05 Turbulentξ/D 0.000226f 0.0152
0.0140Pressure Drop per 1 feet of pipe 0.003714 PsiaDischarge elevation Head 38.00 ftHydrostatic pressure 7.99 PsiaTotal length 583.98 ft∆P in straight pipe 2.1691 PsiaFittings,valves expansion, contraction, etc EquipmentItem Number of item k Item ∆P psiaBall Valve 3 0.126Check Valve 1 0.7 Air cooler 10.15Pipe Entrance 3 2.34 Orifice 2Pipe Exit 3 3 Control valve 20.3
24 10.08 OthersTotal 34 16.246 Total 32.45
∆P through valves and fittings 2.6414 Psia∆P through line 37.2604 PsiaDischarge pressure 410.647 Psia 28.3 barTotal Discharge Head 1955.864 ft 596 mPump Power
ft
90˚ Elbow
B49
figure 2-11 page 68 LUDWIG
Efficiency 83%Pump Horsepower required 160.12 hp 119.40 Kw
Temeprature 60 ˚ C 140Pressure 1.1 bara 15.95Vapor pressure 0.59 bara 8.55
Rate Flow 250 1100.72Viscosity 0.4 CpSP.GR 0.69
Fittings,valves expansion, contraction, etcItem Number of item kBall Valve 1 0.039Gate Valve 1 0.169
5 1.95Sharp Edged Exit 1 0.01Tee 1 0.78Sudden Contraction 1 0.00325
2.948
m3/hr
90˚ Elbow
Total Kt
˚ Fpsiapsia
GPM
