Multistage crosscurrent operations

Multistage Crosscurrent Adsorption The amount of adsorbent required for the separation of a given amount of solute can be decreased by employing multistage crosscurrent contact, which is usually operated in batch mode, although continuous operation is also possible. The required adsorbent is further decreased by increasing the number of stages. However, it is seldom economical to... 

Example 1 In an API manufacture, a stirred tank of 5 m capacity is used as a reactor. It is charged with a solvent and cooled to 5 °C from the ambient temperature. The reactants are added and the reaction is carried about for 8 h under constant stirring. At the end of the reaction, the reaction mixture is washed with the same volume of water at 10 °C and then the wash water is decanted. The washing is repeated 6 times. Then, the vessel is cleaned for the next operation to meet regulatory requirements. The total batch time is about 40 h. Thus the vessel is occupied for 40 h. These washings amount to batch crosscurrent multistage extraction. There is a loss of the API as well as of the solvent (in which the API is held) in each of these washing. The yield is only about 60%. 

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