Bioreactors schematic representation

Fig. 2 Schematic representation of the environmental bioreactor for the antibiotic resistance enrichment...

Figure 13.1 Schematic representation of a fully instrumented bioreactor system for an industrial-scale fed-batch culture (solid line - fluid flow and air flow dotted line - ana-log/digital signals).

FIGURE 47 Schematic representation of the complex multifunctions enabled in a dual membrane bioreactor for hydridoma cell culturing (Integra Biosciences AG, Wallisellen, Switzerland). 

The plastic bag is disposable and is provided sterile by the manufacturer. This makes it a very attractive bioreactor type for production purposes, especially if the production scale is not very large. Since it is not sterilized in-house, there is no need for validation of the sterilization procedure. The validation of bag sterilization is the responsibility of its manufacturer. Since it is not reused, there is no need for cleaning and validation of cleaning procedures. Figure 9.6 (see color section) shows a photograph and a schematic representation of a wave bioreactor. 

Schematic representation of a hollow-fiber bioreactor fitted with an extracapillary recirculation...

Schematic representation of a spin-filter fitted on the impeller shaft of a bioreactor.

Stirred-tank bioreactor with a bubble aeration system (A) schematic representation (B) photograph of a 300 L bioreactor (CIM, Cuba). 

Figure 13.11 Schematic representation of generic perfusion bioreactor.

Figure 13.13 Schematic representation of a wave-mixed disposable bag bioreactor.

Figure 2.22. Schematic representation of the basic experimental situation in bio-process/bioreactor analyses, where the interactions between physical transports (kj ) and biokinetic rates (kh) in the liquid phase are thought to be representative for the process rates in the solid phase of cell mass (kf,). At the same time, response lags of measuring electrodes (k ) have to be taken into account. G, gas phase L, liquid phase S, solid phase or substrate E, enzyme or electrode I, intermediary metabolites or products P, end product N, nucleus R, ribosomes M, mitochondria a, anabolism jS, catabolism Fq = gas flow rate n = agitators rotational speed.

FIGURE 38.1 Schematic representation of several bioreactor configurations used for stem cell culture, (a) Spinner flask (b) stirred suspension bioreactor (c) wave bioreactor and (d) rotating wall vessel. The slow turning lateral vessel (STLV) configuration is shown (e) hollow-fiber bioreactor and (f) packed-bed bioreactor. 

Typical schematic representation of activated sludge process (a) membrane bioreactor (b) conventional activated sludge process. 

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