DaEarl
Chemical
- Sep 7, 2006
- 26
Greetings all,
I am new to the design of pumping systems and in fact I am fresh out of school. Anyways, I am working a project where I must spec out a new booster pump for our products transfer. This booster (vertical 3 stg. turbine) boosts flow to three larger pumps in parallel. These three larger pumps then discharge to the pipeline company and then on to market. The point of the project is to raise our flowrate about 30%. However, this existing booster will run out on its curve at 11000 bbl/h and thus the need for a new pump. Besides the NPSHA & flowrate for the booster, what other conditions might the pump people need? All I can think of is the fluid properties (SG,visc). Or maybe the end conditions (i.e. discharge of booster/suction side of 3 transfer pumps) at the suction side of the three pumps in parallel.
Kyle
I am new to the design of pumping systems and in fact I am fresh out of school. Anyways, I am working a project where I must spec out a new booster pump for our products transfer. This booster (vertical 3 stg. turbine) boosts flow to three larger pumps in parallel. These three larger pumps then discharge to the pipeline company and then on to market. The point of the project is to raise our flowrate about 30%. However, this existing booster will run out on its curve at 11000 bbl/h and thus the need for a new pump. Besides the NPSHA & flowrate for the booster, what other conditions might the pump people need? All I can think of is the fluid properties (SG,visc). Or maybe the end conditions (i.e. discharge of booster/suction side of 3 transfer pumps) at the suction side of the three pumps in parallel.
Kyle