High Pressure Pump

Shigme Vertical Multi-Stage Centrifugal Pump

BL(T) series stainless steel multi-stage centrifugal pump (afterwards called pump) boasts characters of high efficiency, low noise, steady operation, etc. The hydraulic pump set adopts the non-self-priming vertical multi-stage structure, ensuring a compact body, easy installation, convenient operation and maintenance.

Email: info@scclearpure.com

Tel: +86-13699279286 (whatsapp)


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Application Limits of Vertical Pump

  • Medium temperature: normal type: 0℃~68℃ hot water type: 0℃~120℃

  • Ambient temperature: +40℃

  • Max ambient pressure: 1.0MPa

  • Advisable to use motor of higher power in case that the density or viscosity of medium is above that of water.

  • pH: 5 to 8


Application Fields of Centrifugal Pump


     Water supply

BL

BL T

Filtration and transfer at waterworks

Distribution from waterworks

Pressureboosting in mains

Pressure boosting in high-rise buildin g s, hotels, etc.

Pressure boosting for industrial water supply

Industry

 

 

Pressure boosting

Process water systems

Washing and cleaning systems

Vehicle washing tunnels

Fire fighting systems

Liquid transfer

 

 

Cooling and air-conditioning systems(refrigerants)

Boiler feed and condensate systems

Machine tools(cooling lubricants)

Aquafarming

Transfer

Oil and alcohol

Glycol and coolants

Water treatment

 

 

Ultra-filtration systems

Reverse osmosis systems

Softening, ionising, demineralizing systems

Distillation sys tems

Separators

Swimming baths

lrrigation

 

 

Field irrigation(flooding)

Sprinkler irrigation

Drip-feed irrigation


Certificate
CE

Electric Motor

  • Full-enclosed and ventilating two-pole standard motor

  • Protection class: IP55 

  • Insulation class: F

  • Standard voltage Single phase 220V-50Hz Three phase: 380/400V-50Hz

  • Standard motor efficiency: 11kW to 45kW:IE3, other: IE2, specific efficiency value for below table

Energy Efficiency Standard (IEC60034)

Energy.jpg

Calculation of minimum Inlet Pressure
 If the pressure in pump is lower than the vapor pressure of medium, cavitation will occur, which will affect the performance of pump. To avoid the cavitation and ensure the pump inlet has a minimum pressure, maximum suction head should be calculated as below:
 H=Pbx10.2-NPSH-Hf-hv-Hs
 Pb: Atmospheric pressure, bar (In close pipeline system, it can be considered as the system pressure);
 NPSH: Net positive suction head, m (Value at maximum flow of Q-NPSH curve);
 Hf: Suction pipe line loss (Value at maximum flow of corresponding pipeline);
 Hv: Medium vapor pressure, m (Medium vapor pressure at corresponding temperature, the default medium is water, as shown in figure4 on the right);
 Hs: Safety margin, m, general value is 0.5.
 Calculation result: if H is positive, the pump is installed in suction way, otherwise, it is installed in downdraft way.
 Note: It is not necessary to do above calculation under general conditions. Only when we use pump in the following situations do we need to calculate the H:
 1. Medium temperature is high;
 2. The velocity of flow is larger than rated value;
 3. Suction head is big or inlet pipeline is long;
 4. System pressure is small;
 5. Inlet condition is bad.