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NTU Number of Transfer Units

NTU (Number of Transfer Units) The NTU required for a given separation is closely related to the number of theoretical stages or plates required to carry out the same separation in a stagewise or plate-type apparatus. For equimolal counterdiffusion, such as in a binary distillation, the number of overall gas-phase transfer units Nog required for changing the composition of the vapor stream from y to t/2 is [Pg.61]

When diffusion is in one direction only, as in the absorption of a soluble component from an insoluble gas, [Pg.61]

When it is known that H0G varies appreciably within the tower, this term must be placed inside the integral in Eqs. (5-290) and (5-291) for accurate calculations of hT. For example, the packed-tower design equation in terms of the overall gas-phase mass-transfer coefficient for absorption would be expressed as follows  [Pg.61]

In a similar way, liquid-phase mass-transfer rates may be defined by the relations [Pg.61]


NTU Number of transfer units (general) Dimensionless Dimensionless... [Pg.590]

NTU (Number of Transfer Units) The NTU required for a given separation is closely related to the number of theoretical stages or plates required to carry out the same separation in a stagewise or... [Pg.429]


See other pages where NTU Number of Transfer Units is mentioned: [Pg.82]    [Pg.106]    [Pg.548]    [Pg.147]    [Pg.362]    [Pg.674]    [Pg.54]    [Pg.119]    [Pg.159]    [Pg.42]    [Pg.271]    [Pg.578]    [Pg.735]    [Pg.3]    [Pg.374]    [Pg.106]    [Pg.64]    [Pg.269]    [Pg.19]    [Pg.688]    [Pg.1437]    [Pg.557]    [Pg.90]    [Pg.106]    [Pg.698]    [Pg.1434]    [Pg.325]    [Pg.552]   
See also in sourсe #XX -- [ Pg.624 , Pg.647 ]




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