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(i.e. 5.2 <strong>and</strong> 3.04 respectively, please refer to section 3.3.2 <strong>and</strong> 3.3.3). The detailed results<br />

have been discussed in the following sections.<br />

4.2.1 Performance <strong>of</strong> ITDAR during start-up <strong>and</strong> continuous operations<br />

The performance <strong>of</strong> ITDAR for treating the OFMSW with two different C/N ratios (27 <strong>and</strong><br />

32) was evaluated under various organic loading rates using the mesophilic inoculum<br />

sources. The overall recital during initial start-up phase, in association with the OLR <strong>and</strong><br />

Digrr (<strong>digestate</strong> recirculation rate) were measured using parameters like pH, alkalinity,<br />

VFA <strong>and</strong> methane yield as depicted in Figure 4.3(a-e). The results have been discussed in<br />

the following subsections.<br />

a) Monitoring <strong>of</strong> ITDAR during start-up phase<br />

Initial pH <strong>of</strong> the substrate contents within the ITDAR was acidic (5.5–5.8) due to<br />

accumulation <strong>of</strong> very high VFA concentrations <strong>of</strong> 37,857 mg/L, which was mainly<br />

released from the rapid degradation <strong>of</strong> readily available biodegradable components in the<br />

simulated feedstock 1 (Table 4.1; Appendix C, Table C-1). The biogas yield was higher<br />

with the higher CO2 <strong>and</strong> lesser CH4 contents during this period. Therefore, NaOH was<br />

added between 3 rd <strong>and</strong> 6 th day to attain the pH <strong>of</strong> near natural range to support with the<br />

methanogenic activity in ITDAR. With the continuous pH maintenance in ITDAR, it<br />

showed the percentage increase in methane content <strong>of</strong> biogas samples i.e., increased from<br />

3% to 33%, on 10 th day with the alkalinity value <strong>of</strong> 23,000–27,000 mg/L as CaCO3. Also,<br />

the ammonia-N contents were measured in the range <strong>of</strong> 1800–2100 mg/L in ITDAR. The<br />

ORP <strong>of</strong> liquid <strong>digestate</strong>, which was considered as a good indicator <strong>of</strong> <strong>anaerobic</strong> condition,<br />

was measured as -260 mV <strong>and</strong> -450 mV in ITDAR before <strong>and</strong> after pH adjustment. Less<br />

than -300 mV <strong>of</strong> ORP found to be favoring the methanogenesis process in <strong>anaerobic</strong><br />

system was reported by Alkaya <strong>and</strong> Demirer (2011).<br />

Therefore, it was very clear that the ITDAR attained its methanogenesis stage within 14<br />

days <strong>of</strong> batch operations with the continuous pH adjustment, which can be visualized from<br />

the stable pH, ORP <strong>and</strong> methane contents.<br />

b) Monitoring <strong>of</strong> ITDAR during continuous operation phase (Run 1 to 8)<br />

The pH variation in ITDAR during different runs (1–8) has been depicted in Figure 4.3c. It<br />

was observed that, the near neutral pH <strong>of</strong> 7 <strong>and</strong> above was maintained throughout the study<br />

period (<strong>of</strong> 280 days) even with the increasing OLRs (Figure 4.3a) in ITDAR.<br />

The results showed that the system was able to get naturally buffered, which means that the<br />

acid producers <strong>and</strong> acid consumers were equally dynamic, <strong>and</strong> produced specific methane<br />

yield <strong>of</strong> 219 L/kg VSadded on an average from different trials (Figure 4.3d <strong>and</strong> Appendix C,<br />

Table C-2). In other sense, the ITDAR was continuously acting like an active<br />

methanogenic reactor <strong>and</strong> the <strong>waste</strong> fed into the system was comparatively lesser than the<br />

reactor contents, hence the system pH <strong>and</strong> associated methane yield was not getting much<br />

affected with the increasing OLRs. Generally, the methanogenic system pH was reported<br />

to be in between 6.8 <strong>and</strong> 7.8 (Lahav <strong>and</strong> Morgan, 2004).<br />

63

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