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2.6.2 Single-stage continuous systems<br />

In continuous <strong>digestion</strong> process, the <strong>waste</strong> is fed <strong>and</strong> withdrawn from the reactor<br />

continuously. As the substrate is continuously added, all biochemical reactions involved in<br />

the generation <strong>of</strong> biogas occur at a reasonably constant rate. The system receives its weight<br />

little by little, spread over time, so that <strong>digestion</strong> takes place uninterrupted having no end<br />

point. A reasonably constant rate <strong>of</strong> biogas production is resulted by this. Full-scale single<br />

stage continuous <strong>digestion</strong> systems in Europe cover over 87% <strong>digestion</strong> capacity <strong>of</strong><br />

bio<strong>waste</strong> <strong>and</strong> sewage sludge (De Baere, 2006). Industrialists prefer one-stage systems<br />

because <strong>of</strong> their simpler designs <strong>and</strong> lower investment costs. The continuous input<br />

<strong>anaerobic</strong> <strong>digestion</strong> requires less l<strong>and</strong> area <strong>and</strong> its operating cost can be comparable.<br />

Importantly, the higher initial investment cost may be compensated from real state cost<br />

reduction where the l<strong>and</strong> is scarce.<br />

However, a technical difficulty associated with pump has been encountered in loading the<br />

feedstock in continuous manner (Sharma et al. 2000). Mixing is <strong>of</strong> pivotal importance in<br />

all <strong>anaerobic</strong> <strong>digestion</strong> systems, continuous systems rely on pumping for its continuous<br />

operation (Lissens et al , 2001). Further, the continuous system requires high internal<br />

fluidity for the smooth feedstock intake <strong>and</strong> removal process. Such systems are, therefore,<br />

principally suitable for low <strong>solid</strong> <strong>waste</strong>s. For higher <strong>solid</strong> content, transport <strong>and</strong> h<strong>and</strong>ling<br />

<strong>of</strong> the <strong>waste</strong> is carried out with conveyor belts, screws <strong>and</strong> powerful pumps especially<br />

designed for viscous streams. Such types <strong>of</strong> equipment are very expensive (Mata-Alvarez<br />

et al., 2003).<br />

There has been a shift <strong>of</strong> the research focus on semi-continuous mode <strong>of</strong> operation. Semicontinuous<br />

digesters are fed at continuous intervals <strong>of</strong> time, as for example on daily basis,<br />

or on more frequent intervals, with simultaneous removal <strong>of</strong> the <strong>digestate</strong> (Wang et al.,<br />

2003; Misi <strong>and</strong> Forster, 2002). These systems are suited to regularly <strong>and</strong> steadily arising<br />

<strong>waste</strong> stream. The biogas yield <strong>of</strong> semi-continuous processes is characteristically higher<br />

<strong>and</strong> more regular. The higher production rate is attributed to the <strong>waste</strong> that is kept in their<br />

original state, <strong>and</strong> not diluted with water (Ole szkiewicz <strong>and</strong> Poggi-Varaldo, 1997). The<br />

distinction between continuous <strong>and</strong> semi-continuous system is rather subjective. Most <strong>of</strong><br />

the continuous digesters in large scales are not truly continuous. They are operated in semicontinuous<br />

mode (Sharma et al., 2000). The term ‘continuous system’ is used in a broader<br />

sense, which includes truly continuous <strong>and</strong> semi-continuous <strong>digestion</strong> systems where the<br />

digesters are fed once or twice a day.<br />

2.6.3 Multi-stage continuous systems<br />

As <strong>anaerobic</strong> <strong>digestion</strong> process consists <strong>of</strong> four steps <strong>and</strong> each <strong>of</strong> these requires different<br />

conditions for optimal growth <strong>and</strong> function <strong>of</strong> its respective microbial group involved in<br />

the process. For instance, acidogens are more active at relatively low pH (i.e. 5.5–6.0)<br />

while acetogens <strong>and</strong> methanogens require stable neutral pH <strong>and</strong> are sensitive to even low<br />

concentrations <strong>of</strong> inhibitors (e.g., ammonia <strong>and</strong> VFA). Moreover, acetogens also need<br />

close proximity with methanogens for efficient inter-species hydrogen transfer. However,<br />

most full-scale <strong>digestion</strong> systems in use are single-stage digesters, in which all <strong>of</strong> the four<br />

processes have to be carried out simultaneously. In this way, the metabolic activities <strong>of</strong><br />

different microbial groups are compromised <strong>and</strong> the performance <strong>of</strong> single-stage systems is<br />

<strong>of</strong>ten suboptimal with a low reduction <strong>of</strong> VS. Thus, multi-stage system or more<br />

appropriately, two-stage systems were introduced by the researchers to manage <strong>and</strong><br />

23

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