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29<br />

Process flexibility is <strong>on</strong>e of the advantages of multi-stage systems. However,<br />

this flexibility also increases cost <str<strong>on</strong>g>and</str<strong>on</strong>g> complexity by requiring additi<strong>on</strong>al<br />

reactors, material h<str<strong>on</strong>g>and</str<strong>on</strong>g>ling <str<strong>on</strong>g>and</str<strong>on</strong>g> process c<strong>on</strong>trol systems. On the opposite end<br />

of the spectrum, batch or sequential batch systems aim to reduce complexity<br />

<str<strong>on</strong>g>and</str<strong>on</strong>g> material h<str<strong>on</strong>g>and</str<strong>on</strong>g>ling requirements. As opposed to c<strong>on</strong>tinuous wet <str<strong>on</strong>g>and</str<strong>on</strong>g> dry<br />

systems, the feedstock does not need to be carefully metered into a batch<br />

reactor, thereby eliminating the need for complex material h<str<strong>on</strong>g>and</str<strong>on</strong>g>ling<br />

equipment. The primary disadvantage of batch digesters is uneven gas<br />

producti<strong>on</strong> <str<strong>on</strong>g>and</str<strong>on</strong>g> lack of stability in the microbial populati<strong>on</strong>. To surmount these<br />

issues, batch systems can also be combined with multi-stage c<strong>on</strong>figurati<strong>on</strong>s.<br />

Batch Reactors: are loaded with feedstock, subjected to reacti<strong>on</strong>, <str<strong>on</strong>g>and</str<strong>on</strong>g> then are<br />

discharged <str<strong>on</strong>g>and</str<strong>on</strong>g> loaded with a new batch. Substrate is sealed in the digester for<br />

the complete retenti<strong>on</strong> time. When unmixed, the c<strong>on</strong>tent of the digester<br />

stratifies into layers of gas, scum, supernatant, an active layer, <str<strong>on</strong>g>and</str<strong>on</strong>g> stabilized<br />

solids at the bottom. Retenti<strong>on</strong> times range from 30-60 days, with typically an<br />

<strong>organic</strong> loading rate between 0.5 <str<strong>on</strong>g>and</str<strong>on</strong>g> 1.6 kg TVS/m 3 reactor volume/day. There<br />

are three types of batch systems (Figure 12.):<br />

Figure 12.: The (3) types of batch reactors systems<br />

(EPA., 2008)<br />

‣ Single stage batch<br />

‣ Sequential batch system<br />

‣ Up flow Anaerobic Sludge Blanket reactor<br />

The single-stage batch system involves re-circulating the leachate to the top of<br />

the same reactor. An example of such a system is the Biocel process in Lelystad,

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