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Reorienting Waste Remediation Towards Harnessing Bioenergy  243


              deactivates AB (Venkata Mohan, 2010; Zhu and Beland, 2006). Hydroge-
              nase enzyme activity is inhibited at a low or high pH beyond the optimum
              range. The fate of pyruvate depends on the operating pH. Under acidic con-
              ditions pyruvate is converted into VFA along with H 2 by AB. Neutral pH
              operation leads to the formation of CH 4 and CO 2 by MB. Under basic pH,
              anaerobic digestion leads to solventogenesis. Hydrogenase activity is higher
              at an acidic pH, but with an increase in pH, the metabolic pathway proceeds
                                                          +
              to the next step of anaerobic digestion where H get reduced to CH 4
              (methanogenesis) or ethanol (solventogenesis). Accumulation of acid
              metabolites (VFA) during dark-fermentation causes a marked drop in the
              system’s pH, which reduces the buffering capacity, thereby inhibiting the
              H 2 production (Devi et al., 2010; Lin and Lay, 2004b). The pH range of
              5.5–6.0 is optimum to avoid both methanogenesis and solventogenesis
              and can be considered as a manipulated variable for the process control,
              especially for dark-fermentation process (Venkata Mohan et al., 2007d,
              2010b). A longer fermentation period induces a metabolic shift from acid-

              ogenesis to methanogenesis, which is considered to be unfavorable for H 2
              production. Maintaining a shorter retention time, between 8.0 and 14 h,
              therefore helps to restrict the MB growth as well as activity (Hawkes
              et al., 2007; Venkata Mohan, 2010, Venkata Mohan et al., 2007a–d,
              2008d,f, 2011a; Vijaya Bhaskar et al., 2008). Methanogens can be suppressed
              by maintaining short retention time (2–10 h) as AB grow faster (Fang and
              Liu, 2002; Nakamura et al., 1993; Ren et al., 2005; Venkata Mohan,
              2009; Zhu and Beland, 2006).
                 Nitrogen at optimal concentration is beneficial for H 2 production,
              while at higher concentrations it can inhibit the process performance by
              affecting the intracellular pH of the bacteria or by inhibiting specific
              enzymes related to H 2 production (Bisaillon et al., 2006; Chen et al.,
              2008; Salerno et al., 2006). The optimal nitrogen concentration of
              0.1 g N/L was found to have a positive effect on H 2 production and sub-
              strate degradation (Wang et al., 2009). An ideal carbon-to-nitrogen (C/N)
              ratio helps in bacterial growth and affects H 2 production by both mixed
              and pure cultures. A C/N ratio of 47 has been shown to affect fermentative
              H 2 production by mixed microorganisms (Lin and Lay, 2004a). Wastewa-
              ter that is low in carbon content can be combined with materials high in N
              to attain the desired C:N ratio of 30:1 (Yadvikaetal.,2004). Wastewater
              with excess nitrogenous compounds and ammonia inhibits nitrogenase
                                                           2+
              activity (Redwood and Macaskie, 2006). Iron (Fe )isveryimportant
              for the function of hydrogenase and also acts as an active site component
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