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Generation of bioenergy from industrial waste using microbial fuel cell technology  187

           8.5.1 Microbial fuel cell configurations and designs

           Many researchers have been examined for increasing the power output of MFCs,
           focusing areas such as altering MFC designs, cost-effective electrodes, electrode
           modification, and membranes for enhancing surface area of the electrode and their
           actions in order to overcome the difficulties in e 2  and H 1  transport system. The
           schematic of MFC is shown in Fig. 8.1. In anode chamber, microorganisms act as
           electrochemically active bacteria to oxidize the substrates through PEM. These e 2
                1
           and H travel to the cathode through an external electrical device, and it diffused
           through electrolyte and PEM. With platinum as a catalyst, protons and electrons are
           joined at the cathodic chamber with oxygen to form H 2 O. Numerous configurations
           and shapes of MFCs have been developed to run in batch, fed-batch, or continuous
           mode operation. A two-staged MFC setup consists of an anode and a cathode com-
           partment separated by a PEM such as Nafion. In recent times, single-chambered
           MFC (SC-MFC) has gained considerable attention, because cathode is in direct con-
           tact with the atmosphere as shown in Fig. 8.2. Since open air-cathode systems can
           be used in SC-MFCs, they are quite attractive for their increasing power production
           efficiency. Nevertheless, a lot of SC-MFCs still use Nafion or PEM membrane for
           separating the electrons and protons.
              A considerable increase in transfer of oxygen in anodic section in absence of a
           PEM was reported, whereas two-chambered MFCs can have a wide range of appli-
           cations even with a relatively low power output. Cathodic denitrification is such a
           good example. This design has outstanding applications in industrial effluent treat-
           ment due to its effortless scale-up, proton transfer problems, etc. Nevertheless, oxy-
           gen back diffusion is a dangerous disadvantage that is comparatively higher than in




























           Figure 8.1 Schematic representation of dual-chambered microbial fuel cell.
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