I did removal of total volatile fatty acid (acetic and butyric acids) from waste water in batch study using shake flask. After that I transfer the optimized parameter (pH, adsorbent dosage and contact time) to a fixed bed column. My objective is to optimize the removal of these acids in batch study without optimizing the parameter for the column (due to cost constraint and other major research objective). What are the possible changes that one can expect from the changes in the system's configuration especially in term of interaction between the adsorbate and adsorbent (isotherm).

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