ChemE2912
Chemical
- Jul 11, 2003
- 26
I need to select an ANSI pump for a water treatment plant, with the following problem:
According to the Process data we have calculated, the pump differential and flow rate, we have to select a 1x1.5 pump (outlet x inlet nozzle diameters).
However, due to the nature of the fluid we are handling (water + suspended solids) and requirements of our client, our suction line is 3".
Then, in order to interconnect the pump with this pipe, a 3x1.5 reducer is required and the velocity in the reducer and inlet nozzle is too high (22 ft/s).
According to API14E, the velocity should not exceed an erosional limit (in this case 20.25 ft/s).
Also, this reducer introduces a high pressure drop (due to the kinetic and frictional terms).
We have tried to find a pump with bigger inlet and outlet nozzles, without success.
Is there any harm in the pump and/or these fittings if we maintain this or higher velocities?
Regards,
Alberto
According to the Process data we have calculated, the pump differential and flow rate, we have to select a 1x1.5 pump (outlet x inlet nozzle diameters).
However, due to the nature of the fluid we are handling (water + suspended solids) and requirements of our client, our suction line is 3".
Then, in order to interconnect the pump with this pipe, a 3x1.5 reducer is required and the velocity in the reducer and inlet nozzle is too high (22 ft/s).
According to API14E, the velocity should not exceed an erosional limit (in this case 20.25 ft/s).
Also, this reducer introduces a high pressure drop (due to the kinetic and frictional terms).
We have tried to find a pump with bigger inlet and outlet nozzles, without success.
Is there any harm in the pump and/or these fittings if we maintain this or higher velocities?
Regards,
Alberto