Do Not specify Head as Maximum 16 bar
Specify the Operating Pressure
Pump Manufacturer may specify Maximum Working pressure as 16 bar on the catalogue
but it does not mean that the pump can operate with a discharge pressure of 16 bar
A pump with a discharge pressure of 8 bar and 16 bar .makes a huge difference in term
of Pump Size & the Motor KW
As I had always mentioned if you are not sure of the Discharge Head ,check the Guages of existing unit or Calculate
Also .when you increase flow for the same diameter of pipeline,the discharge head increases as well
For Bulking Installation ,pumping for factories to Ship the pipeline is usually quite long ,
and this is make a huge difference in pumping head
Suction Line is equally important , as pumps are located at Pumping Station a distant away
from the Tank Farm .When level in the tank drop ,the NPSH avialable is the system will also
drop . Cavitation will take place .One way of ditecting is looking at the running ampheres
28.11.08
21.11.08
VELOCITY IN PUMPING
For new pumps and piping projects , especially for high viscous products it is necessary to
working out the velocity of flow before deciding on the pipe size (most will straight away decide on the pipe size )
The ideal velocity for discharge line should be between 1 to 3 meter per second
and suction between 0.5 to 1.5 Meter /sec
Higher velocity means smaller pipe being used ,thus higher head loss and this mean pump
operates at higher pressure , and higher head means higher Kw of drive or bigger size of pump
On the cost factor , the piping cost will be lower but power cost will be higher
Work out total cost of piping for different size and compare with power cost and see the saving achieveable
This is applicable to high capacity pumping rate . small pumps will not affect much
Suction line is usually more critical .There is one bulking plant where suction line diameter
is to small and pump located far away from tankyard , all these resulted in extremley low NPSH
avialable , at 0.20 meter . Any upgrading of pump is not possible to achieve the required capacity as any pump will be operate in cavitating condition . Replacing the suction line system will cost a bomb .
Looking at this comparison , a pump operating at 9 bar and another at 6 bar
model : 200-500 -------------------------200-500
capacity : 450 m3/hr at 9 bar ------------450 m3/hr at 6 bar
motor Kw : 150 Kw ----------------------95 Kw
See the huge difference in motor kw ( 60% )?
working out the velocity of flow before deciding on the pipe size (most will straight away decide on the pipe size )
The ideal velocity for discharge line should be between 1 to 3 meter per second
and suction between 0.5 to 1.5 Meter /sec
Higher velocity means smaller pipe being used ,thus higher head loss and this mean pump
operates at higher pressure , and higher head means higher Kw of drive or bigger size of pump
On the cost factor , the piping cost will be lower but power cost will be higher
Work out total cost of piping for different size and compare with power cost and see the saving achieveable
This is applicable to high capacity pumping rate . small pumps will not affect much
Suction line is usually more critical .There is one bulking plant where suction line diameter
is to small and pump located far away from tankyard , all these resulted in extremley low NPSH
avialable , at 0.20 meter . Any upgrading of pump is not possible to achieve the required capacity as any pump will be operate in cavitating condition . Replacing the suction line system will cost a bomb .
Looking at this comparison , a pump operating at 9 bar and another at 6 bar
model : 200-500 -------------------------200-500
capacity : 450 m3/hr at 9 bar ------------450 m3/hr at 6 bar
motor Kw : 150 Kw ----------------------95 Kw
See the huge difference in motor kw ( 60% )?
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