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Adsorption process in batch system was carried out by varying pH, initial U VI) concentration, adsorbent dose, adsorption time and temperature.
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The photodegradation tests in the batch system were carried out without membrane changing the characteristic variables of the process (light intensity, TiO2 concentration, 4NP concentration, O2 concentration, pH) to find their optimum values.
The first selection experiment with the Serratia systems was carried out in static batch culture microcosms (25 cm Sarstedt flasks with 15 ml of NAS [New Cereal Leaf - Page's modified Neff's amoebae saline] medium at 25°C.
Considering a full-scale application in an agricultural context, a batch test was carried out to evaluate the performance of the system.
Batch fermentation was carried out in a 2 L BIOSTAT® Bplus stirred tank reactor (Sartorius Stedim System GmbH, Guxhagen, Germany) with a working volume of 1.5 L.
Each batch test was carried out at least in triplicate.
Each autotrophic batch cultivation was carried out in duplicate.
Repeated batch culture was carried out by continuously repeating different cycles of batch culture at same time interval.
The fed-batch fermentation was carried out in a 5-L stirring bioreactor (Bio Control and System, Daejeon, Korea) with a working volume of 3 L.
Digestion for two parallel batches each per sample was carried out in an Ultra CLAVE III digestion system (MLS GmbH. Leutkirch, Germany) at 240 °C.
The phenomenological modeling approach based on unstructured and non-segregated kinetic models was formulated to describe PHB synthesis by Cupriavidus necator that experimentally was carried out in batch system for the given temperatures of 30; 32.5; 35 and 37.5 °C.
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