Deear All,
Thank you for the contributes;
the problem was a real gardening problem, however data are not available;
If you like, consider the following pump as reference:
Output: 1 HP,
Outlet: 2"
Rated: H 7.5 (M), Q 220 (L/M)
Maximum: H 12 (M), Q 450 (L/M)
Dimension: 350 L x 162 W x...
Thanks for the contributes, I don't have specific data for the garden pump:
Supposing the following partial further information available:
Impeller Diameter: 200mm
Number of Vanes: 10
Approach Angle of Vanes:5%
Numero di stadi:1
Many Thanks,
Max
Thank you for your answer;
There is the need of a further clarification: my question is how to evaluate a priori if the pump can do it ( given the flow-rate )?
Thanks
Max
Dear All,
More than a process engineering question, it could be considered a gardening problem.
How to determine the Centrifugal Pump Head for a given flowrate without using a Pressure Gauge? ( Characteristic Curves are not available )
Best regards,
Max
I would be interested in knowing both the cases:
1) No Heat Trasfer to Fluid ( is there an analytical solution ? )
2) No heat transfer from the outside surroundings
thanks
Dear All,
I need to determine the Vessel Wall Temperature after Gas depressurization trough an orifice ( API 521 ) and to verify the necessity of applying Low Temperature Carbon Steel. I know the possibility of using Hysys ( ASPEN Tech. )Depressurization Utility, however I have the following...
Dear All,
I need to determine the Wall Vessel Temperature after Gas depressurization trough an orifice ( API 521 ) and to verify the necessity of applying Low Temperature Carbon Steel. I know the possibility of using Hysys ( ASPEN Tech. )Depressurization Utility, however I have the following...