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As a case study, sequencing batch reactor was selected to examine the suggested procedure.
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The Williams Otto semi-batch reactor was selected as case study, since its model formulation can be represented by two different set of states: (a) a mass basis states set and (b) a mass fraction basis states set.
The batch reactor was equipped with air pump for aeration and a magnetic stirrer for agitation.
A 15-l sequencing batch reactor was inoculated with biomass from the WWTP Lieshout.
Mixing in a macro-scale batch reactor is usually achieved by stirring.
A hydrophobic reactor surface was selected for this synthesis to avoid MNPs nucleation on the reactor walls, thus preventing reactor fouling and uncontrolled particle growth.
A semi-batch reactor was employed to produce the O3 aq) solution [29].
A batch reactor integrated with a pervaporation unit was selected as the model system.
Batch reactors are a useful tool to improve understanding of the outcomes of anaerobic digestion processes.
The most efficient isolate was selected and characterized, together with both POP and the parental strain (PAR), in a batch reactor with 60% (v/ v) undetoxified HSSL.
The DonnaII reactor and ANAS semi-batch reactor were maintained as described previously [ 19, 20].
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