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24<br />

If the proper c<strong>on</strong>diti<strong>on</strong>s cannot be maintained, imbalances am<strong>on</strong>g the different<br />

types of microorganisms in the process will occur. One of the most comm<strong>on</strong><br />

problems is the buildup of <strong>organic</strong> acids which kills the methanogenic<br />

organisms <str<strong>on</strong>g>and</str<strong>on</strong>g> gives even more acidity to the process envir<strong>on</strong>ment. Produced<br />

acid can be c<strong>on</strong>trolled in a natural way by using inherent chemical buffers <str<strong>on</strong>g>and</str<strong>on</strong>g><br />

by the methanogens themselves as they c<strong>on</strong>sume acids to produce methane.<br />

These c<strong>on</strong>trols cannot c<strong>on</strong>fr<strong>on</strong>t the difficulties if too much feed is added <str<strong>on</strong>g>and</str<strong>on</strong>g><br />

<strong>organic</strong> acids are produced faster than they are c<strong>on</strong>sumed, if inhibitory<br />

compounds accumulate, or if the feed stream lacks natural pH buffers such as<br />

carb<strong>on</strong>ate <str<strong>on</strong>g>and</str<strong>on</strong>g> amm<strong>on</strong>ium. (EPA.,2008)<br />

Solids c<strong>on</strong>centrati<strong>on</strong> higher than about 40% TS can also result in process<br />

inhibiti<strong>on</strong>, likely due to the reduced c<strong>on</strong>tact area available to the AD<br />

microorganisms. The c<strong>on</strong>tent of TS in the MSW typically ranges from (30-60)<br />

%, this is the reas<strong>on</strong> why water needs to be added each time this problem<br />

occurs. Process water can be used, but this may also result in the buildup of<br />

inhibitory compounds. Thus, low-solids digesters require the additi<strong>on</strong> of fresh<br />

water. In higher temperatures which occur to smaller reactors a given <strong>waste</strong><br />

stream is needed to be processed. However, the micro-organisms themselves<br />

are adapted to relatively narrow temperature ranges. Mesophilic <str<strong>on</strong>g>and</str<strong>on</strong>g><br />

thermophilic microbes are adapted to roughly 30-40°C <str<strong>on</strong>g>and</str<strong>on</strong>g> 50-60°C<br />

respectively. (EPA., 2008)<br />

2.2.5. AD stages<br />

Generally the overall AD process (Figure 10.) can be divided into four stages:<br />

Pretreatment, <strong>waste</strong> digesti<strong>on</strong> , gas recovery <str<strong>on</strong>g>and</str<strong>on</strong>g> residue treatment.<br />

Most digesti<strong>on</strong> s y s t em s require pretreatment of <strong>waste</strong> to obtain<br />

homogeneous feedstock. The preprocessing involves separati<strong>on</strong> of n<strong>on</strong>digestible<br />

materials <str<strong>on</strong>g>and</str<strong>on</strong>g> shredding. The <strong>waste</strong> received by AD digester is<br />

usually source separated or mechanically sorted. The separati<strong>on</strong> ensures<br />

removal of undesirable or recyclable materials such as glass, metals, st<strong>on</strong>es<br />

etc. In source separati<strong>on</strong>, recyclables are removed from the <strong>organic</strong> <strong>waste</strong>s<br />

at the source. If source separati<strong>on</strong> cannot be achieved, mechanical<br />

separati<strong>on</strong> could occur even though the final product hasn’t got the same<br />

quality because it is not as clean as in source seperati<strong>on</strong>.The <strong>waste</strong> is shredded<br />

before it is fed into the digester. Inside the digester, the feed is diluted to<br />

achieve desired solids c<strong>on</strong>tent <str<strong>on</strong>g>and</str<strong>on</strong>g> remains in the digester for a designated<br />

retenti<strong>on</strong> time. (Verma.,2002)

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