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Tower operating pressure, optimization

Typically, the air-stripper manufacturer will supply liquid flow ranges acceptable for a particular tower. Selecting an air stripper for which the design flow is at the lower end of the tower s rated capacity will produce high contaminant removal rates, but may not optimize power requirements. For large-scale systems where significant operational costs may be incurred by overdesigning the system, the use of pressure-drop curves and calculations such as Eqs. (1)-(13) are required. [Pg.54]


See other pages where Tower operating pressure, optimization is mentioned: [Pg.25]    [Pg.304]    [Pg.443]    [Pg.55]    [Pg.354]    [Pg.72]    [Pg.115]    [Pg.90]    [Pg.73]    [Pg.197]    [Pg.640]    [Pg.2587]    [Pg.692]    [Pg.652]    [Pg.430]    [Pg.66]    [Pg.774]    [Pg.138]    [Pg.74]   


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