PalomaP
Mechanical
- May 11, 2007
- 23
An horizontal Between Bearing, Axially Split, Single Stage Pump @ 1000m3/h, 38m, 1480 rpm, 119 kw (impeller 368 mm). The system curve is H=26+12.10^-6.q^2
When changing duty conditions to (500 m3/h, 29m) checking online pumps charts, changing speed impeller to 1200 rpm, new power is 52,4 kw (ef.75,3%). However changing the impeller diameter to 310 mm, new power is 55,2 (ef.71,6%).
Why this difference in the efficiency? changing speed or diamater should be the same...(according to affinity laws).
In stead of using curves program on line from the supplier, how could i use the affinity laws? How can i check the values of new impeller diameter or new speed for new conditions?
Thanks in advance
When changing duty conditions to (500 m3/h, 29m) checking online pumps charts, changing speed impeller to 1200 rpm, new power is 52,4 kw (ef.75,3%). However changing the impeller diameter to 310 mm, new power is 55,2 (ef.71,6%).
Why this difference in the efficiency? changing speed or diamater should be the same...(according to affinity laws).
In stead of using curves program on line from the supplier, how could i use the affinity laws? How can i check the values of new impeller diameter or new speed for new conditions?
Thanks in advance