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Inter-pass absorption towers

The temperature of circulating oleum at the inlet of the tower plays a very important role in the proper absorption of the SO3 from the gas phase. It is maintained as low as possible—and generally not allowed to exceed 52-53 °C. There is a considerable escape of acid mist from the oleum tower and hence it is almost always followed by an acid tower (the inter-pass absorption tower). [Pg.24]

In the earlier variants of the DCDA process, the SO2 was converted to SO3 by catalyst passes and the SO3 was then absorbed in the inter-pass absorption tower. The gases from the exit of the IPAT were again reheated to about 425 35 °C and... [Pg.54]

Separate acid circulation circuit for final absorption tower to avoid stripping of dissolved SO2 from the inter-pass absorption tower acid circuit which can occur if a common acid circulation tank is used. [Pg.98]

The following details should be separately recorded for each of the acid towers (drying tower, inter pass absorption tower, final absorption tower)... [Pg.128]


See other pages where Inter-pass absorption towers is mentioned: [Pg.11]    [Pg.11]   
See also in sourсe #XX -- [ Pg.11 , Pg.12 , Pg.14 , Pg.20 , Pg.24 , Pg.54 , Pg.55 , Pg.59 , Pg.63 , Pg.67 , Pg.68 , Pg.73 , Pg.82 , Pg.98 , Pg.99 , Pg.105 , Pg.120 , Pg.122 , Pg.128 ]




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Absorption towers

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