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Gambar hm cyclone 
overflow discharge 
(atmospheric pressure) 
CYCLONE 
underflow discharge 
(atmospheric pressure) 
underflow discharge 
(atmospheric pressure) 
P required = 135-180 kPa P required = 135-180 kPa 
0.5 m 
3 m 
1 15.5 
3 
PUMP 
pipe section 1 
pipe section 3 
pipe section 2 
pipe section 4 
HEAVY MEDIUM PUMP CALCULATION 
Data New Pump Worn Pump 
Flowrate required, Q (m3/hr) 830 680 
Flowrate required, Q (l/s) 230.556 188.889 
Flowrate required, Q (m3/s) 0.231 0.189 
Solid S.G 2.2 2.2 
Slurry S.G 1.47 1.47 
Head produced (m slurry) 30 26 
Suction line 
Suction pipe length l (m) 3 3 
Suction pipe diameter, Ds (m) 0.300 0.300 
Suction pipe diameter, ds (mm) 300 300 
Smaller suction pipe dia (m) 0.203 0.203 
Smaller suction pipe dia (mm) 203 203 
Total suction line equivalent length (m) 3 3 
Discharge Line 
Length of pipe l (m) 16.8 16.8 
Total long radius bend (each) 0.500 0.500 
Total tee (each) 0.250 0.250 
Equivalenth length from 90 long radius bend 2 2 
Equivalenth length from tee 2.875 2.875 
Total discharge line equivalent length L (m) 21.675 21.675 
Discharge pipe inside diameter d (mm) 300 300 
Discharge pipe inside diameter D (m) 0.300 0.300 
Smaller discharge pipe inside diameter d1 (mm) 203 203 
Smaller discharge pipe inside diameter D1 (m) 0.203 0.203 
Suction pipe diameter, Ds (m) 0.300 0.300 
Suction pipe diameter, ds (mm) 300 300 
Suction head Zs (m) 2 2 
Discharge head Zd (m) 16.3 16.3 
Friction value f 0.020 0.020 
Gravitation g (m/s2) 9.810 9.810 
Slurry velocity at pipeline, V (m/s) 3.261 2.672 
Slurry velocity at smaller dia at discharge, V1 (m/s) 7.122 5.835 
Slurry velocity at suction pipe, Vs (m/s) 3.261 2.672 
Friction head for discharge pipeline, Hfd (m) 0.783 0.526 
Friction head for suction pipe line, Hfs (m) 0.108 0.073 
Loss in discharge pipe enlargement, He (m) 0.418 0.281 
Loss at pipe discharge Hv (m) 0.542 0.364 
Loss at entrance to suction, Hs (m) 0.271 0.182 
Head loss due to sudden enlargement (m) 0.760 0.510 
Head loss due to suddent contraction (m) 0.043 0.029 
Total slurry head, Hm (m) 17.226 16.264 
Residual head 12.774 9.736 
Cyclone pressure (kPA) 184.213 140.402 
Total head of the system (m slurry) 30 26

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hm cyclone

  • 1. Gambar hm cyclone overflow discharge (atmospheric pressure) CYCLONE underflow discharge (atmospheric pressure) underflow discharge (atmospheric pressure) P required = 135-180 kPa P required = 135-180 kPa 0.5 m 3 m 1 15.5 3 PUMP pipe section 1 pipe section 3 pipe section 2 pipe section 4 HEAVY MEDIUM PUMP CALCULATION Data New Pump Worn Pump Flowrate required, Q (m3/hr) 830 680 Flowrate required, Q (l/s) 230.556 188.889 Flowrate required, Q (m3/s) 0.231 0.189 Solid S.G 2.2 2.2 Slurry S.G 1.47 1.47 Head produced (m slurry) 30 26 Suction line Suction pipe length l (m) 3 3 Suction pipe diameter, Ds (m) 0.300 0.300 Suction pipe diameter, ds (mm) 300 300 Smaller suction pipe dia (m) 0.203 0.203 Smaller suction pipe dia (mm) 203 203 Total suction line equivalent length (m) 3 3 Discharge Line Length of pipe l (m) 16.8 16.8 Total long radius bend (each) 0.500 0.500 Total tee (each) 0.250 0.250 Equivalenth length from 90 long radius bend 2 2 Equivalenth length from tee 2.875 2.875 Total discharge line equivalent length L (m) 21.675 21.675 Discharge pipe inside diameter d (mm) 300 300 Discharge pipe inside diameter D (m) 0.300 0.300 Smaller discharge pipe inside diameter d1 (mm) 203 203 Smaller discharge pipe inside diameter D1 (m) 0.203 0.203 Suction pipe diameter, Ds (m) 0.300 0.300 Suction pipe diameter, ds (mm) 300 300 Suction head Zs (m) 2 2 Discharge head Zd (m) 16.3 16.3 Friction value f 0.020 0.020 Gravitation g (m/s2) 9.810 9.810 Slurry velocity at pipeline, V (m/s) 3.261 2.672 Slurry velocity at smaller dia at discharge, V1 (m/s) 7.122 5.835 Slurry velocity at suction pipe, Vs (m/s) 3.261 2.672 Friction head for discharge pipeline, Hfd (m) 0.783 0.526 Friction head for suction pipe line, Hfs (m) 0.108 0.073 Loss in discharge pipe enlargement, He (m) 0.418 0.281 Loss at pipe discharge Hv (m) 0.542 0.364 Loss at entrance to suction, Hs (m) 0.271 0.182 Head loss due to sudden enlargement (m) 0.760 0.510 Head loss due to suddent contraction (m) 0.043 0.029 Total slurry head, Hm (m) 17.226 16.264 Residual head 12.774 9.736 Cyclone pressure (kPA) 184.213 140.402 Total head of the system (m slurry) 30 26