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dry anaerobic digestion of municipal solid waste and digestate ...

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Total ammonia-N to total nitrogen ratio (TAN/TKN ratio) is considered as a good indicator<br />

for estimating the percentage conversion <strong>of</strong> total nitrogen into ammonia-N during the<br />

<strong>anaerobic</strong> <strong>digestion</strong>. As stated, the calculated percentage <strong>of</strong> ammonia-N with the feedstock<br />

1 was around 0.77, whereas, it was 0.40 for the feedstock 2. Kayhanian (1999) suggested<br />

that using feedstock C/N ratio from 27 to 32 promotes steady digester operation at<br />

optimum ammonia-N levels. In the present study, feedstock 2 with C/N ratio 32 produced<br />

an overall less concentration <strong>of</strong> ammonia-N <strong>and</strong> free ammonia as compared to feedstock 1.<br />

Moreover, there was no accumulation <strong>of</strong> ammonia-N under commonly used retention time<br />

(20–30 days) for digesters. Thus the feedstock with C/N ratio 32 was found to be better<br />

than that with C/N ratio 27 for <strong>dry</strong> thermophilic <strong>anaerobic</strong> <strong>digestion</strong> to minimize or avoid<br />

ammonia-N inhibition.<br />

In our experiment, Feedstock 2 had low %TKN (1.62%), which produced TAN 1993<br />

mg/L. Using these two values, mathematical calculation for Feedstock 1 having high<br />

%TKN (1.92%) was done, by which it should produce TAN 2350 mg/L (Expected TAN).<br />

But in actual experiment, it produced even higher TAN, i.e., 2821 mg/L. Thus<br />

experimental value <strong>of</strong> TAN production for <strong>waste</strong> with high %TKN (or low C/N ratio) was<br />

higher than its calculated value (Expected TAN). The reason may be that the system was<br />

biological but not stoichiometric. The presence <strong>of</strong> high amount <strong>of</strong> %TKN in case <strong>of</strong><br />

feedstock 1 (C/N 27) as compared to C/N 32 might have resulted a relatively rapid growth<br />

<strong>of</strong> microbes, which in turn resulted in the more conversion <strong>of</strong> organic nitrogen into TAN.<br />

Thus experimental TAN was higher than Expected TAN in case <strong>of</strong> feedstock 1. However,<br />

it needs to be proved experimentally in future studies.<br />

From the results <strong>of</strong> this experiment, it can be concluded that ammonia nitrogen<br />

accumulation (one main operational problem <strong>of</strong> <strong>dry</strong> <strong>anaerobic</strong> <strong>digestion</strong>) can be thus<br />

mitigated by use <strong>of</strong> correct feed mixture (i.e. by adjusting composition or C/N ratio <strong>of</strong> the<br />

feed). ii) This method to mitigate ammonia accumulation is good for <strong>dry</strong> <strong>anaerobic</strong><br />

<strong>digestion</strong> as the other methods (dilution <strong>of</strong> ammonia by addition <strong>of</strong> water as well as<br />

stripping <strong>of</strong> ammonia) are not desirable <strong>and</strong>/or suitable for <strong>dry</strong> <strong>digestion</strong>. iii) Moreover,<br />

adjusting the feed composition can be easily managed for a decentralized <strong>dry</strong> AD system<br />

compared to centralized system.<br />

4.2.4 Energy balance <strong>of</strong> ITDAR in Phase I pilot experiment<br />

Table 4.2 compiled the net energy gains obtained from two different trials <strong>of</strong> ITDAR <strong>and</strong><br />

most <strong>of</strong> the runs produced surplus energy. The net energy gain from the reactor is<br />

determined by the quality <strong>of</strong> produced biogas. The quality <strong>of</strong> biogas, in turn, depends on<br />

the operational conditions <strong>and</strong> feedstock composition. Please refer to Appendix E for<br />

methodology <strong>of</strong> energy balance calculations.<br />

Average energy consumptions during different runs were distributed as 75% for<br />

maintaining the reactor under thermophilic conditions, 12% for the shredding, 2.5% for the<br />

<strong>waste</strong> loading <strong>and</strong> withdrawal <strong>and</strong> 9.6% for the <strong>digestate</strong> recirculation. From the energy<br />

consumption percentile, it was evident that the continuous temperature maintenance <strong>of</strong> the<br />

ITDAR upset with the maximum percentage <strong>of</strong> net energy gained.<br />

70

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