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Could the experts recommend a pump with a low net positive suction head? Thank you!

2017-10-09View Original

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I need a pump with a low net positive suction head requirement – an axial flow pump or a centrifugal pump – with a flow rate of 30 m3/h, a head of 3 m, and a net positive suction head of less than 1.5 m. Please recommend some options, thanks!
Reply #22017-10-09
With such a low net positive suction head, neither of these two pumps will be able to meet it. I’m wondering why you need such a low net positive suction head under your operating conditions
Reply #32017-10-09
I’m quite troubled because a small crystallization skid-mounted testing setup needs to be designed, and its height is limited
Reply #42017-10-09
Where do you calculate that the net positive suction head should be less than 1.5M?
Reply #52017-10-09
The backflow feeding issue should be easy to resolve; you can refer to the following measures. Measures to prevent cavitation: To avoid cavitation, it is necessary to increase NPSHa so that NPSHa > NPSHr. The measures to prevent cavitation are as follows: a) Reduce the geometric suction head hg (or increase the geometric backflow height);     b. Reduce the suction loss hc; this can be achieved by increasing the pipe diameter, minimizing the length of the pipelines, as well as reducing the use of elbows and other fittings ;    c. Prevent operation at high flow rates for extended periods of time ;    d. At the same speed and flow rate, a double-suction pump is used, as it reduces the inlet flow velocity and thus makes cavitation less likely to occur ;   e. When cavitation occurs in the pump, the flow rate should be reduced or the pump should operate at a lower speed ;   f. The conditions of the pump suction tank have a significant impact on pump cavitation ;    g. For pumps operating under harsh conditions, to avoid cavitation damage, cavitation-resistant materials can be used.
Reply #62017-10-10
Using a low-speed centrifugal pump can achieve levels below 1.5 meters! No problem at all. I checked the company’s information!
Reply #72017-10-10
Hello! I checked the data for low-speed centrifugal pumps (1450 rpm), and the NPSH value is also around 2.5 meters
Reply #82017-10-10
It’s better to raise the tank height; the required net positive suction head for the pump is generally around 2 meters, so there’s no need to make things too complicated
Reply #92017-10-10
It’s just that there’s a height limit; otherwise, there wouldn’t be such a dilemma.:)

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