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PUMPS for  Process Industries Ranjeet Kumar M.Tech - Chemical
Equation of Energy  ,[object Object],[object Object],[object Object],Impeller Rotating Part Volute Static Part
Types of Pumps ,[object Object],[object Object],[object Object],[object Object],[object Object]
Basis for selection of Pump ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],>>>Capacity & Head required are most important selection criteria and  define size of the pump.
Capacity  ,[object Object],[object Object],[object Object],[object Object],[object Object]
Centrifugal Pump Design Problem ,[object Object],[object Object],[object Object],[object Object],Benefits of Centrifugal Pumps – low cost, easy maintenance, wide selection, & simple design.
Head of Pump ,[object Object],[object Object],[object Object]
Physical Properties Consideration ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Solid content ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Fig – Types of Impeller
[object Object]
Site Conditions ,[object Object],[object Object],[object Object]
Selection of Pump –  Capacity & Head < 200 cSt < 25 m Upto 1 m 3 /h Peristaltic > 2% < 25% < 600 cSt 10500 m < 300 m 3 /h Positive Displacement > 2% < 5% Max  1050 m < 350 m 3 /h Rotary < 2% Upto 20% < 200 cSt Upto 105 m Upto 7500 m 3 /h Centrifugal % Gas Solid Viscosity Head Capacity Type
Flow Rate Design ,[object Object],PFD indicates normal flow rate without any margin & the Maximum flow is  Considered for sizing of the pump with margin 30% Waste Heat Boiler pump 25% Boiler Feed water pump 0% Recirculation pump 3-5% Large cooling water pump 0-5% Transfer pumps 0% Intermittent pumps 20-25% Reflux pumps 10% Continuous process pumps Margin Service
[object Object],[object Object]
Static Head  ,[object Object],[object Object],[object Object],1.0 Above 200 0.9 100 – 200 0.7 0 – 100 Pump centre line above ground Flow Rate (m 3 /h)
Line Pressure Drop ? ,[object Object]
Pressure Drop for Control Valve ,[object Object],[object Object],[object Object],[object Object],[object Object]
Pressure Drop for Devices 0 Ultrasonic & electromagnetic Flow Meter 0.2 – 0.4 Corilolis Flow Meter 0.2 – 0.4 Vortex 0.02 – 0.05 Venturi Flow Meter 0.25 Orifice Flow meter 0.07 bar (continuous strainer) Y, T or Bucket type Strainer 1.0 bar Air cooler 0.35 – 0.5 bar per shell 0.7 bar per pass in tube side Shell & Tube type Heat Exchanger Press Drop (in bar) Devices in Flow Line
NPSH ,[object Object],[object Object],[object Object],[object Object],[object Object]
NPSHA  optimization ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],NPSHR  Rotary  <  NPSHR  Centrifuge  <  NPSHR  Reciprocating
Efficiency ,[object Object],[object Object],[object Object],[object Object]
Seals, pumps curves ,[object Object]

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Pumps for Process Industries

  • 1. PUMPS for Process Industries Ranjeet Kumar M.Tech - Chemical
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  • 10. Fig – Types of Impeller
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  • 13. Selection of Pump – Capacity & Head < 200 cSt < 25 m Upto 1 m 3 /h Peristaltic > 2% < 25% < 600 cSt 10500 m < 300 m 3 /h Positive Displacement > 2% < 5% Max 1050 m < 350 m 3 /h Rotary < 2% Upto 20% < 200 cSt Upto 105 m Upto 7500 m 3 /h Centrifugal % Gas Solid Viscosity Head Capacity Type
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  • 19. Pressure Drop for Devices 0 Ultrasonic & electromagnetic Flow Meter 0.2 – 0.4 Corilolis Flow Meter 0.2 – 0.4 Vortex 0.02 – 0.05 Venturi Flow Meter 0.25 Orifice Flow meter 0.07 bar (continuous strainer) Y, T or Bucket type Strainer 1.0 bar Air cooler 0.35 – 0.5 bar per shell 0.7 bar per pass in tube side Shell & Tube type Heat Exchanger Press Drop (in bar) Devices in Flow Line
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