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Off Nozzle Elevation

The value of H- is useful when elevation adjustments are made to vessel heights during plant layout or when the vessel can be located at a minimum elevation. The coefficient for P2 in the above equation is the elevation difference between the downcomer and rizer nozzle. If this is other than 3 feet, the correct dimension, in feet, should be inserted. [Pg.248]

The downcomer nozzle cannot be lower than Hx. Af replaces AP in the above equation and is the sum of the downcomer pipe, riser and exchanger friction losses  [Pg.248]

Many towers have a bottom draw-off pump. NPSH requirements usually elevate the process [Pg.248]

For the minimum of downcomer length the return line nozzle elevation H ) must be known. Inserting H2 = Hi + H3 into the AP equation and solving for Hi  [Pg.249]

Af is again the sum of the actual resistances of the reboiler plus the downcomer and riser pipe plus the inlet and outlet losses at the vessel and exchanger. [Pg.249]


See other pages where Off Nozzle Elevation is mentioned: [Pg.248]    [Pg.250]    [Pg.252]   


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