Vertical Multi-Stage Centrifugal Pump

Product Detail

Overview Of The Product

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

Application Limits

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

Applications Fields




Water supply	BL	BLT
Filtration and transfer at waterworks
Distribution from waterworks
Pressureboosting in mains
Pressure boosting in high-rise buildins,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









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)



Calculation Of minimum Inlet Pressure

If the pressure in pump is lower than the vapour 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 following:

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 vapour pressure, m (Medium vapour 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.



Selection Of Pumps

Selection of pumps should be based on:

1. Duty point of the pump.

2. Dimensional data such as pressure loss as aresult of height differences,friction loss in the pipework,

3. Pump efficiency etc. 

4. Pump materials

5. Pump connections 

6. Commonly used mechanical seal configuration tables

1. Duty point of the pump:

From a duty point it is possible to select a pump onthe basis of the curve charts shown in "performancecurves/technical" data.

2. Dimensional data:

When sizing a pump the following must be takeninto accounting:  

·Required flow and pressure at the draw-off point.

·Pressure loss as a result of height differences.

·Friction loss in the pipework(Hf) (Refer to Fig.1) It may.

·Best efficiency at the estimated duty point.

·NPSH value.

·For calculation of the NPSH value, see correspondingcurves chart.

3. Pump efficiency:

Before determining the best efficiency point, the operation pattern of the pump needs to be identified. If the pump expected to operate as the same duty point, then select a BL pump which is operating at a duty point corresponding with the best efficiency of the pump.

As the pump is sized on the basis of the highest possible flow, it is important always to have the duty point to the right on the efficiency curve(eta)in order to keep efficiency high when the flowdrops.



4. Pump material:

The material variant should be selectedbased of the liquid to be pump.BL wetted parts are made of AISI304BLT pump body is made of cast-iron and .

Wetted parts are made of AISI304.

5. Pump connections 

Selection of pump connection depend on the rated pressure and pipe work. the pump offer a wide range of ftexible connection such as:

·Pipe thread

·Oval flange

·DIN flange

·Other connections on reguest

6. Commonly used mechanical seal configuration tables

Configuration	Configuration illustrate	Application Field	Configuration case
EUBV	Container-type E,hard alloy moving ring U,Static ring leaching resin graphite B, fluorine rubber V	1. Working condition regular under cold water 0 ? to 68 ?  , no particles, oil. 2. Working condition regular under hot water 68 ? to 90 ?  , no particles,with oil.	Normal
EQQE	Container type E, moving ring and static ring silicon carbide Q , epdm E	Working condition:hot water 90 ? to 120 ? , containing a small amount of particles, no oil.	Normal
EQQV	Container type E,moving ring and static ring silicon carbide  Q, fluorine rubber V	1. PH = 5-7 acidic medium. 2. PH = 7-9, alkaline medium. 3. Working conditions: hot water   68 ? to 90 ?, containing a small  amount of particles, oil. 4. With oil.	Customer-made
EUUE	Container type E, moving ring and statil ring U, hard alloy U, epdm E	1. Under ice water 0? . 2. A crystallization of alkaline medium. 3. Containing a large number of granular media. 4. More than 2 MPa pressure condition.   5. No oil.	Customer-made

Maximum Work Pressure




Model	Curve No.
BL(T)2,4	2
BL(T)8,12,16,20	3
BL(T)32-2-2~BL(T)32-7	1
BL(T)32-8-2~BL(T)32-12	4
BL(T)32-13~BL(T)32-15-2	5
BL(T)45-2-2~BL(T)45-6	1
BL(T)45-7-2~BL(T)45-9	4
BL(T)45-10-2~BL(T)45-13-2	5
BL(T)64-2-2~BL(T)64-5-2	1
BL(T)64-5-1~BL(T)64-8	4
BL(T)90-2-2~BL(T)90-4-2	1
BL(T)90-4~BL(T)90-6	4






The limits of pressure and temperature are shown in the following fig.4,the pressure and temperature must be in the shown in the fig. 

4.Maximum Ambient Temperature

When the pump is operating in the place where ambient temperature is 

higher than 40? or altitude is higher than 1000m,the output power of motor 

P2 will decrease because of poor cooling caused by low air density.Therefore,

in that case,the pump should be equipped with high-power motor.



Performance Range



Product Range