01/07/2025
HOW NPSHa IS CALCULATED BY CHEMICAL PROCESS ENGINEERS IN PLANT DESIGN
The are 3 main information a chemical process engineer must defined for the correct quotation and purchase of a pump: rated flow, rated head and NPSHa. There is other relevant information to be informed in the datasheet, but let's focus on the NPSHa for this post.
In a few words, NPSHa is the pressure of the liquid at the pump suction minus the v***r pressure of the liquid at the operating temperature. The results of this calculation, plus a safety margin, must be higher than the NPSHr.
But how to define the pressure of the liquid at the pump suction?
Besides the source fluid composition, associated with pressure and temperature, leading to the fluid properties. The NPSHa is strongly influenced by the elevation of the fluid in relation to the pump suction. This elevation, by its hands, depends on the stage of the project.
At the Conceptual Design phase, there is no pump (project-specific curve of performance) information available. In many cases, vessel elevation is defined based on minimum values used by Design Companies. No plot plant or layout is available, so it is not possible to perform a detailed pressure drop calculation. NPSHa at this stage is an estimation.
In Basic Engineering, usually, the plot plant is available. This way, it is possible to have better information about the location of the vessel and the pump. Allowing the pressure drop calculation up to the pump suction. If any pump quotation is available, the vessel elevation is still preliminary. So the NPSHa is preliminary.
In the Detailing Engineering Phase, the pump curve for the project (vendor selection) is finally available. Based on that, the vessel elevation can be confirmed or will need to be revised to comply with the pump NPSHr. At this stage, it is possible to calculate the "final" NPSHa for the pump.