Abstract

The effect of organic loading rate (OLR) on a pressurized anaerobic filter was studied in a laboratory two-phase anaerobic digestion system. The anaerobic filter was operated successively at two working pressures (9 bar and 1.5 bar). The OLR(COD) for each pressure was increased from 5 to 17.5 kg·m−3·day−1. The best performance of the reactor at 9 bar was observed at OLR(COD) of 12.5 kg·m−3·day−1 and hydraulic retention time (HRT) of 1.8 day, with specific biogas productivity (SBP) of 5.3 L·L−1·day−1 and COD degradation grade of 90.6%. At higher OLRs and shorter HRTs, the process became unstable. In contrast, there was no indication of digester failure during the experiments at 1.5 bar. The SBP peaked at OLR(COD) of 17.5 kg·m−3·day−1 with 8.2 L·L−1·day−1, where COD degradation grade was 90.4%. The biogas collected from the reactor at 9 bar and 1.5 bar contained approximately 74.5% CH4 and 66.2% CH4, respectively, regardless of OLR variation. At OLR(COD) of 5–12.5 kg·m−3·day−1, the reactor at 9 bar had the same specific methane yield as at 1.5 bar, which was in the range of 0.31–0.32 LN·g−1COD. Raising the working pressure in the reactor resulted in an increase of methane content of the produced biogas. However, the low pH value (approximately 6.5) inside the reactor, induced by high CO2 partial pressure seemed to limit the reactor performance at high OLRs and short HRT.

Highlights

  • Biogas, an important renewable energy source, is produced through the process of anaerobic digestion of biodegradable substances

  • The leachate from the leach-bed reactors that was used as substrate for the pressurized anaerobic filter underwent corresponding slight changes in acid composition as well as chemical oxygen demand (COD) concentration (Table 3)

  • 12.5 kgCOD·m−3·day−1 and 1.8 d could be taken as the critical organic loading rate (OLR) and hydraulic retention time (HRT) for the anaerobic filter running at 9 bar, where the reactor was characterized by high specific methane productivity (SMP) and specific methane yield (SMY), high reduction in COD and high alkaline buffer capacity

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Summary

Introduction

An important renewable energy source, is produced through the process of anaerobic digestion of biodegradable substances. It is primarily comprised of methane (CH4) and carbon dioxide (CO2). With a large portion of CO2, the utilization of biogas is limited due to its low calorific value. After the proper purification, drying and pressurization, the biogas can be even directly injected into existing natural gas pipelines or used as fuel for vehicles [1]. This further widens the range of biogas application and increases the overall energy utilization efficiency

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