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26<br />

C<strong>on</strong>siderati<strong>on</strong>s such as the design <str<strong>on</strong>g>and</str<strong>on</strong>g> feedstock, give different technical<br />

choices, such as batch or c<strong>on</strong>tinuous flow, vertical or horiz<strong>on</strong>tal orientati<strong>on</strong>,<br />

<str<strong>on</strong>g>and</str<strong>on</strong>g> capacity, total solids c<strong>on</strong>tent, number of stages, mixing <str<strong>on</strong>g>and</str<strong>on</strong>g> pre-treatment.<br />

Digester processes are c<strong>on</strong>structed for meeting specific c<strong>on</strong>diti<strong>on</strong>s, design,<br />

locati<strong>on</strong>s, types of <strong>waste</strong>, <str<strong>on</strong>g>and</str<strong>on</strong>g> the desired degree of aut<strong>on</strong>omy <str<strong>on</strong>g>and</str<strong>on</strong>g> complexity.<br />

Vertical tanks are gravity driven, the material flowing generally downward,<br />

though the path can vary, depending <strong>on</strong> interior boundaries in the chamber. In<br />

other cases, material is pumped into the bottom of the tank <str<strong>on</strong>g>and</str<strong>on</strong>g> removed from<br />

the top, causing general upward flow accompanied by a lesser, downward,<br />

gravity driven flow. Horiz<strong>on</strong>tal tanks require greater space <str<strong>on</strong>g>and</str<strong>on</strong>g> are closer to<br />

plug flow than to perfect mixing. (Buekens.,2005)<br />

2.2.6. Categories of Engineered AD Systems<br />

(V<str<strong>on</strong>g>and</str<strong>on</strong>g>evivere et al.,2002) categorizes the (MSW AD) systems into 3 main<br />

categories :<br />

‣ One-stage C<strong>on</strong>tinuous Systems<br />

Low-solids or ‘Wet’<br />

High-solids or ‘Dry’<br />

Dry-Wet<br />

Wet-Wet<br />

‣ Two-stage C<strong>on</strong>tinuous Systems<br />

‣ Batch Systems<br />

One Stage<br />

Two Stage<br />

(EPA., 2008)<br />

Single-stage digesters: are c<strong>on</strong>sidered to be simple in design, build, <str<strong>on</strong>g>and</str<strong>on</strong>g><br />

operati<strong>on</strong> <str<strong>on</strong>g>and</str<strong>on</strong>g> are generally less expensive. The <strong>organic</strong> loading rate (OLR) of<br />

single-stage digesters is limited by the ability of methanogenic organisms to<br />

tolerate the sudden decline in pH that results from rapid acid producti<strong>on</strong><br />

during hydrolysis.<br />

Two-stage digesters separate the initial hydrolysis <str<strong>on</strong>g>and</str<strong>on</strong>g> acid-producing<br />

fermentati<strong>on</strong> from methanogenesis, which allows for higher loading rates but<br />

requires additi<strong>on</strong>al reactors <str<strong>on</strong>g>and</str<strong>on</strong>g> h<str<strong>on</strong>g>and</str<strong>on</strong>g>ling systems.

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