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Performance and Kinetic Evaluation of Palm Oil Mill Effluent (POME) Digestion in a Continuous High Rate Up-Flow Anaerobic Sludge Blanket (UASB) Bioreactor

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In this study, we operated a 10 litre upflow anaerobic sludge blanket (UASB) reactor continuosly at mesophilic temperature (38 °C). UASB reactor performance was evaluated based on the impact of the hydraulic retention time (HRT) ranged between 1 and 5 days and influent COD concentration in the range of 4540 mgL-1 and 20,820 mgL-1. The pH of the UASB was maintained in the range of 6.5 to 7.2 by adding buffering solution containing of 5 gL-1 of calcium oxide (CaO) derived from waste cockle shells. A simplified Monod’s model was employed to describe kinetics of anaerobic digestion of POME by using UASB reactor at organic loading rates (OLR) in the range between 1.17 g.CODL-1d-1 and 17.22 g.CODL-1d-1. A high COD degradation rate of 93.26 % was recorded at OLR of 3.92 g.COD L-1d-1 and HRT of 4 days. The UASB reactor generated the maximum biogas production at 34.95 L/d when operated at HRT 1 day and OLR 7.70 g.CODL-1. The proposed kinetic equations are applicable to describe anaerobic treatment of palm oil mill effluent with the UASB reactor. Biokinetic coefficients evaluated were, the growth yield (YG), 3.906 g VSS/g CODremoved.d-1; the specific biomass decay (b), 0.233 d-1; the specific biomass growth rate (μmax), 1.861 d-1; and the saturation constant (Ks), 3.459 g-CODL-1.
Title: Performance and Kinetic Evaluation of Palm Oil Mill Effluent (POME) Digestion in a Continuous High Rate Up-Flow Anaerobic Sludge Blanket (UASB) Bioreactor
Description:
In this study, we operated a 10 litre upflow anaerobic sludge blanket (UASB) reactor continuosly at mesophilic temperature (38 °C).
UASB reactor performance was evaluated based on the impact of the hydraulic retention time (HRT) ranged between 1 and 5 days and influent COD concentration in the range of 4540 mgL-1 and 20,820 mgL-1.
The pH of the UASB was maintained in the range of 6.
5 to 7.
2 by adding buffering solution containing of 5 gL-1 of calcium oxide (CaO) derived from waste cockle shells.
A simplified Monod’s model was employed to describe kinetics of anaerobic digestion of POME by using UASB reactor at organic loading rates (OLR) in the range between 1.
17 g.
CODL-1d-1 and 17.
22 g.
CODL-1d-1.
A high COD degradation rate of 93.
26 % was recorded at OLR of 3.
92 g.
COD L-1d-1 and HRT of 4 days.
The UASB reactor generated the maximum biogas production at 34.
95 L/d when operated at HRT 1 day and OLR 7.
70 g.
CODL-1.
The proposed kinetic equations are applicable to describe anaerobic treatment of palm oil mill effluent with the UASB reactor.
Biokinetic coefficients evaluated were, the growth yield (YG), 3.
906 g VSS/g CODremoved.
d-1; the specific biomass decay (b), 0.
233 d-1; the specific biomass growth rate (μmax), 1.
861 d-1; and the saturation constant (Ks), 3.
459 g-CODL-1.

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