Countercurrent flow of gas and water in perforated plates

2000 ◽  
Vol 38 (5) ◽  
pp. 777-782
Author(s):  
S. B. Alekseev ◽  
Yu. N. Ilyukhin ◽  
V. O. Kukhtevich ◽  
S. V. Svetlov ◽  
V. G. Sidorov
1986 ◽  
Vol 51 (11) ◽  
pp. 2489-2501
Author(s):  
Benitto Mayrhofer ◽  
Jana Mayrhoferová ◽  
Lubomír Neužil ◽  
Jaroslav Nývlt

A model is derived for a multi-stage crystallization with cross-current flows of the solution and the crystals being purified. The purity of the product is compared with that achieved in the countercurrent arrangement. A suitable function has been set up which allows the cross-current and countercurrent flow models to be compared and reduces substantially the labour of computation for the countercurrent arrangement. Using the recrystallization of KAl(SO4)2.12 H2O as an example, it is shown that, when the cross-current and countercurrent processes are operated at the same output, the countercurrent arrangement is more advantageous because its solvent consumption is lower.


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