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Pumping Systems and Performance

The specific speed of a given type pump must not exceed the specific speed values presented by the Hydraulic Institute [17]. This is based on a known or [Pg.197]

Depending upon the corrosive or scaling nature of the liquid in the pipe, it may be necessary to take this condi- [Pg.197]

Applied Process Design for Chemical and Petrochemical Plants [Pg.198]

The values of friction loss (including entrance, exit losses, pressure drop through heat exchangers, control valves and the like) are hSL and hDL. The total static head is D -SL, or [(D + D ) — (—SL)] if siphon action is ignored, and [(D + D ) — (S L)] for worst case, good design practice. [Pg.198]

Calculate the friction losses hSL and hDL for three or more arbitrarily chosen flow rates, but rates which span the area of interest of the system. [Pg.198]


See other pages where Pumping Systems and Performance is mentioned: [Pg.197]    [Pg.641]    [Pg.197]   


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