Abstract

A sudden pH drops always inhibits the anaerobic digestion (AD) reactor for biogas production from palm oil mill effluent (POME). The pH adjustment of POME by oil palm ash addition and the biogas effluent recycling effect on the preventing of pH drop and change of the archaea community was investigated. The pH adjustment of POME to 7.5 increased the methane yield two times more than raw POME (pH 4.3). The optimal dose for pH adjustment by oil palm ash addition was 5% w/v with a methane yield of 440 mL-CH4/gVS. The optimal dose for pH adjustment by biogas effluent recycling was 20% v/v with a methane yield of 351 mL-CH4/gVS. Methane production from POME in a continuous reactor with pH adjustment by 5% w/v oil palm ash and 20% v/v biogas effluent recycling was 19.1 ± 0.25 and 13.8 ± 0.3 m3 CH4/m3-POME, respectively. The pH adjustment by oil palm ash enhanced methane production for the long-term operation with the stability of pH, alkalinity, and archaea community. Oil palm ash increased the number of Methanosarcina mazei and Methanothermobacter defluvii. Oil palm ash is a cost-effective alkali material as a source of buffer and trace metals for preventing the pH drop and the increased methanogen population in the AD process.

Highlights

  • Palm oil mill effluent (POME) is the main wastewater generated from palm oil extraction plants, which has a low pH (4.9), high chemical oxygen demand (COD) (68 g/L), and high oil content (6.2 g/L) [1]

  • The anaerobic digestion (AD) of POME is usually operated at high hydraulic retention time (HRT) and low organic loading rate (OLR) to prevent pH drops and fast acidification leading to the requirement of a large reactor volume [3]

  • The drawback of biogas effluent recycling by reducing organic loadings due to the wastewater was diluted by the volume of biogas effluent

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Summary

Introduction

Palm oil mill effluent (POME) is the main wastewater generated from palm oil extraction plants, which has a low pH (4.9), high chemical oxygen demand (COD) (68 g/L), and high oil content (6.2 g/L) [1]. The AD of POME is usually operated at high hydraulic retention time (HRT) and low organic loading rate (OLR) to prevent pH drops and fast acidification leading to the requirement of a large reactor volume [3]. The current commercial biogas reactors size of 6000–10,000 m3 are constructed at most of the oil palm extraction plants to save the construction cost and land used, leading to a low HRT of 10–25 days for reactor operation, corresponding to a POME flow rate of 400–600 m3/d. The variation of feedstock composition and high organic loading operation of readily biodegradable POME can drop the pH in the AD reactor resulting in a low pH inhibition [1]. Adjustment of the pH of the AD reactor to near-neutral is often applied to enhance the buffering capacity of the AD system against VFA accumulation, with low cost and smooth operation [6]

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