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Moreover, from the comparison <strong>of</strong> start-up phases <strong>of</strong> the two pilot experiments, it was<br />

found that low <strong>digestate</strong> recirculation rate (i.e. 1 Ldig/Lreactor vol.d) should be used to achieve<br />

stable reactor conditions in less time. The results <strong>of</strong> continuous loading phase have been<br />

presented in the following sections.<br />

% <strong>of</strong> Biogas<br />

70<br />

60<br />

50<br />

40<br />

30<br />

20<br />

10<br />

0<br />

Methane Carbon dioxide GPR<br />

1 11 21 31 41<br />

Time (days)<br />

Figure 4.8 CH4, CO2 <strong>and</strong> GPR fluctuation during start-up phase<br />

4.3.2 Stability parameters <strong>of</strong> ITDAR: Effect <strong>of</strong> organic loading rate<br />

i) pH<br />

pH is very basic parameter to describe the stability <strong>of</strong> <strong>anaerobic</strong> <strong>digestion</strong>. With OLR <strong>of</strong><br />

4.55 kg VS/m 3 /d, the system stabilized its pH at around 7.75 with a range <strong>of</strong> 7.5-8 as<br />

shown in Figure 4.9. When the OLR was increased from 4.55 to 6.4 kg VS/m 3 .d, pH fell<br />

down to 7.58 <strong>and</strong> regulated to an average <strong>of</strong> 7.67 (7.33 -7.96). As a result <strong>of</strong> further<br />

increase in OLR to 8.5 kg VS/m 3 /d, a drastic decrease in pH was observed <strong>and</strong> pH dropped<br />

to the value <strong>of</strong> 6.89 (Appendix D, Table D-1). Therefore, NaOH was added during days<br />

150-155 to control pH. The decline in pH in the starting days <strong>of</strong> each <strong>of</strong> the first two runs<br />

<strong>and</strong> most <strong>of</strong> the last run is linked to destabilization <strong>of</strong> the system as a result <strong>of</strong> increase in<br />

OLR. The reason is that when organic loading rate is increased, the acidogens also increase<br />

their activity <strong>and</strong> produce high amount <strong>of</strong> VFA, as they are fast growing. But, on the other<br />

h<strong>and</strong>, methanogens owing to their slow specific growth rate can not utilize all the already<br />

produced VFA <strong>and</strong> need more time to build the required population size. Thus initial <strong>and</strong><br />

temporary decrease in pH is due to accumulation <strong>of</strong> VFA as a result <strong>of</strong> this imbalance in<br />

the microbial groups, which is recovered until methanogens build their sufficient<br />

population. The decrease <strong>of</strong> pH is more pronounced while working with higher OLR, i.e.,<br />

8.5 kg VS/m 3 .d. The reason is that the imbalance between acidogenic <strong>and</strong> methanogenic<br />

activity is more pronounced.<br />

ii) Volatile fatty acids (VFA)<br />

The concentration <strong>of</strong> volatile fatty acids in the <strong>digestate</strong> <strong>of</strong> ITDAR was quite stable at an<br />

average value <strong>of</strong> 5100 mg/L (range: 4400-5700 mg/L) while operating at OLR <strong>of</strong> 4.55 kg<br />

VS/m 3 /d (Figure 4.10 <strong>and</strong> Appendix D, Table D-1). When OLR was increased to 6.40 kg<br />

VS/m 3 /d, VFA concentration started to increase <strong>and</strong> reached a maximum value <strong>of</strong> 6500<br />

mg/L with an average value <strong>of</strong> 5400 mg/L in this run. Finally, at OLR <strong>of</strong> 8.50 kg VS/m 3 /d,<br />

74<br />

2.5<br />

2.0<br />

1.5<br />

1.0<br />

0.5<br />

0.0<br />

GPR (L/Lreactor vol./d)

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