open impeller slurry pump replacement

Pump_and_Line_Calc.xls

Economic Analysis

Company NameProject Name Project Number Sheet 1 of 1 Address REV DATE BY APVD REV DATE BY APVD Pump and Line Calculation Sheet Form XXXXX-YY-ZZ Owner's Name Plant Location Case Description Equipment label Equipment name Plant section Process service Fluid Density kg/m3 Operating temperature Normal ºC Viscosity N.s/m2 Min ºC Normal flow rate kg/s Max ºC Design flow rate kg/s LINE PRESSURE DROP SUCTION DISCHARGE Line size mm Line size mm Note Normal Max.Units Note Flow Normal Max.Units u1 Velocitym/s u2 Velocitym/s Df1 Friction loss 0.00 kPa/m Df2 Friction loss 0.00 kPa/m L1 Line length m L2 Line length m Df1 L1 Line loss 0.00 kPa Df2L2 Line loss 0.00 0.00 kPa Entrance losskPa Orifice / Flow meter kPa (40 kPa)Strainer kPa Control valve kPa (1) Sub-totalkPa Equipment S&THX H 205 kPa z1 Static head m kPa 0.0 0.0 kPa kPa Upstream equipment pressure kPa Total(6) Dynamic loss 0 0 kPa (2) Sub-total 0.0 0.0 kPa z2 Static head m (2) - (1)(3) Suction pressurekPa 0.0 0.0 kPa (4) Vapor pressure kPa Equip. press (max)kPa (3) - (4)(5) NPSH available0.0 kPa Contingency 0 0 kPa (5)/rg NPSH availablem(7) Sub-total 0.0 0.0 kPa NPSH available0.0 m water(7) + (6)Discharge pressure 0.0 0.0 kPa (3)Suction pressure0.0 kPa (8) Differential pressure0.0 kPa (8)/rg Pump headm Control valve Valve/(6)% Dyn. loss PUMP DATA Pump manufacturer Driver type Catalog No.Power supply Pump flow rate normalm3/h Seal type max.m3/h Hydraulic powerkW Differential pressurekPa Rated power kW m Efficiency% m water Suction specific speed NPSH required m Pump type Casing design pressure kPa No. of stages Casing design temperature ºC Impeller type Casing type Mounting Casing material SKETCH NOTES 1. 2. 3. 4. 5.