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2.5 THE ANAEROBIC BAFFLED REACTOR<br />

The <strong>anaerobic</strong> <strong>baffled</strong> <strong>reactor</strong> is a high rate <strong>anaerobic</strong> digester that has been used to pre-treat or codigest<br />

high strength or toxic industrial effluents. Its application in the treatment <strong>of</strong> low-strength<br />

wastewaters has been tested on a laboratory-<strong>scale</strong> and in a number <strong>of</strong> full-<strong>scale</strong> applications for the<br />

primary treatment <strong>of</strong> <strong>domestic</strong> wastewater. A modified ABR forms the central unit <strong>of</strong> the DEWATS<br />

(DEcentralised WAstewater Treatment Systems) plant that has been implemented to provide low cost<br />

<strong>domestic</strong> wastewater treatment in low income communities in South-East Asia, India, China and<br />

Africa (Sasse, 1998; BORDA, 2008).<br />

Figure 2.7: Diagram <strong>of</strong> an <strong>anaerobic</strong> <strong>baffled</strong> <strong>reactor</strong> (ABR) showing hanging and standing<br />

baffles. Curved arrows indicate liquid flow, while straight arrows represent gas<br />

production.<br />

The ABR is similar in design and application to the upflow <strong>anaerobic</strong> sludge blanket (UASB) <strong>reactor</strong>,<br />

but it is reported that no special granule formation is necessary for its operation (Barber and Stuckey,<br />

1999). The first <strong>baffled</strong> digesters to be called ABR were described by Bachmann et al. (1985).<br />

The ABR has alternating hanging and standing baffles (Figure 2.7), which divide it into<br />

compartments, and direct liquid flow through a series <strong>of</strong> upward and downward passes. A sludge bed<br />

accumulates through the settling <strong>of</strong> solids in the bottom <strong>of</strong> each compartment, and the liquid flow is<br />

forced through this blanket as it passes under each hanging baffle. Good contact between wastewater<br />

flow and active biomass is ensured by this design. In principle, all phases <strong>of</strong> the <strong>anaerobic</strong> degradation<br />

process can proceed simultaneously in each compartment. However, the sludge in each compartment<br />

will differ depending on the specific environmental conditions prevailing and the compounds or<br />

intermediates to be degraded (Barber and Stuckey, 1999).<br />

The hydrodynamics and degree <strong>of</strong> mixing that occur within a <strong>reactor</strong> <strong>of</strong> this design strongly influence<br />

the extent <strong>of</strong> contact between substrate and micro-organisms, thus controlling mass transfer and<br />

potential <strong>reactor</strong> performance. Micro-organisms within the <strong>reactor</strong> rise and settle depending on flow<br />

direction (up or down) and velocity, particle settling velocity and gas production. Their rate <strong>of</strong><br />

movement along the <strong>reactor</strong> from compartment to compartment is generally slow. The main driving<br />

force behind <strong>reactor</strong> design has been to enhance the solids retention capacity. (Barber and Stuckey,<br />

1999)<br />

The reported advantages <strong>of</strong> the <strong>baffled</strong> <strong>reactor</strong> design are as follows (Barber and Stuckey, 1999):<br />

• The <strong>reactor</strong> design is simple, with no moving parts or mechanical mixing.<br />

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