Figure 1. Pristine membrane permeability at different TMP.
Figure 2. Permeate flux trend during immobilization with different TMP.
Figure 3. Effect of different TMP on membrane observed rejection.
Figure 4. Linear fitting results of experimental permeate flux at different transmembrane pressure according to fouling model by Hermia.
Table 1. Description of four empirical models by Hermia
Table 2. Characteristics of ultrafiltration membrane used in the study
Table 3. Water permeability of pristine membrane at different transmembrane pressure
Table 4. Enzyme loading percentage after immobilization on membrane at different TMP
Table 5. Values of R2 from the model fitting accuracy for the ultrafiltration of ADH solutions at 1, 2 and 3 bar
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