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Additionally, apart from high-speed pumps, it is not recommended to use an inducer wheel to prevent cavitation
This post was last edited by zeq521fcy on 2018-10-25 15:06 for help
I don’t understand; in production, one just needs to use the items as designed according to the instructions. If additional functional equipment is required, it should be done in accordance with the original design’s operating procedures. Why does such a question even arise?
The addition of an inducer wheel results primarily in a change in the pump’s net positive suction head curve; generally, the curve changes from its original shape to a \"saddle-shaped\" one, with both the net positive suction head at low flow rates and high flow rates increasing. As a result, the operating range becomes narrower
I understand there are two aspects: first, the impact on the cavitation margin curve, as mentioned by the brother upstairs; second, the impact on the flexibility of the entire shaft system. The use of an impeller in horizontal pumps increases the weight of the cantilevered section, and this increased weight leads to instability in the shaft system’s deflection, which in turn affects the lifespan of the mechanical seals and bearings. This is also why the use of an impeller is recommended only in vertical high-speed pumps.
This post was last edited by 3983596_FPPZ on 2018-10-25 at 16:39. The impeller design is based on the rated flow rate; when the pump operates at high or low flow rates, the designed flow velocity of the impeller does not match the actual flow velocity of the liquid – it may be either higher or lower. Additionally, the angle of the impeller blades does not correspond to the actual direction of the fluid flow, which causes the blades to exert forces on the liquid, resulting in unstable turbulence and disturbances at the inlet of the impeller. This leads to an increase in the net positive suction head available at that flow rate. The pump can only operate near the design flow rate of the impeller; if the flow rate deviates too much from this value, the pump’s net positive suction head will increase, preventing the pump from functioning properly. Therefore, the impeller narrows the range of flow rates at which the pump can operate. Reducing the effective flow rate range of the pump is a drawback of the impeller; when designing the impeller, the pump’s rated flow rate should not be used as a reference, but rather the actual process flow rate at the site, in order to avoid this problem. Furthermore, in operating conditions with large fluctuations in flow rate, impellers are not suitable for use; after all, to date there have been no impellers, like those found in some high-flow pumps, whose blades can be adjusted in angle. Hope this can help you
I’m not quite sure what exactly the so-called “scope of work” refers to