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32    Energy from Toxic Organic Waste for Heat and Power Generation


          for optimum biogas production. Therefore, it is often necessary to period-
          ically monitor the pH of digester to keep track of the changes in alkalinity
          throughout the anaerobic digestion process.
             Gupta et al. [57] investigated the biogas production in batch reactors,
          with detoxified Mahua seed cake as feedstock. They observed that the di-
          gester containing cattle dung and water in the ratio 1:1 gives a pH range
          between 6.4 and 7.2. On the other hand, the digesters containing cake
          mixtures showed an initial decrease in the pH (5.9–6.1) for about 6–9 days,
          indicating a fast hydrolytic and acetogenic phase, and then moved toward
          the alkaline range.
             Desai  and  Madamwar  [58]  reported  that  the  amount  of  CO 2   and
          volatile fatty acids produced during anaerobic digestion affect the pH of
          the digester slurry. For a smoother anaerobic digestion, the concentration
          of volatile fatty acids and acetic acid in the feedstock should be below
          2000 mg/L.

          Hydraulic Retention Time
          It is the average time consumed by the input feedstock inside the digester
          before it comes out after digestion. Generally, the HRT depends upon the
          tropical climate condition. A shorter retention time is likely to face the risk
          of less active bacterial action, while a longer retention time requires a larger
          volume of the digester, and hence, a higher capital investment.
             Baserja  [59] observed a maximum gas production of 2.2  L/day
          (CH 4  = 62%) at an HRT of 10 days having a loading rate of 6 g TS/L,
          while treating a mixture of cattle dung, poultry waste, and cheese with
          ratio of 2:1:3. The retention time ranges between 30 and 60 days, and
          only about 1/3 of the tank volume is used for active digestion. If an-
          aerobic digestion is to be completed with other MSW (municipal solid
          waste) disposal options, then the retention time must be lower than the
          current standard of 20 days. Garba [50] indicated that, for mesophilic di-
          gestion, the temperature range varies from 25°C to 40°C and the HRT
          may be longer than 20 days.


          Solid Concentration
          The amount of raw materials fed into the digester depends upon the solid
          concentration. Desai and Madamwar [58] documented their investigation
          results related to biogas production from cheese whey, poultry waste, and
          cattle dung. They observed that the best acceptable solid concentration for
          a faster anaerobic digestion was in the range of 7%–9%. The total solid level
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