Full Length Research Paper
Abstract
An investigation on biohydrogen production from palm oil mill effluent (POME) was conducted in a continuous stirred tank reactor seeded with polydimethyl-siloxane (PDMS) immobilised mixed cultures at adjusted retention time. The hydrogen-producing bacteria obtained from an anaerobic digester used for treating POME were acclimatised and immobilised in PDMS. The immobilised cultures were assessed for their effectiveness in generating hydrogen in a continuous system. In this study, the PDMS cultures were fed with raw POME at hydraulic retention times of 6, 4 and 2 days and operated at controlled pH and temperature of 5.5 and 55°C, respectively. At hydraulic retention time (HRT) 2 days, the average hydrogen production rate per unit volume of POME was 2.1 NL/L/d. Hydrogen constituted up to 43% of the total gas produced and methane was not detected throughout the 150 days of continuous operation. The soluble carbohydrate degradation efficiency was highest at 81.2% during HRT 4 days and the concentration of soluble metabolites produced, followed the order of acetic > butyric > ethanol > propionic acid. The microbial diversity of the immobilised consortia determined by denaturing gradient gel electrophoresis (DGGE) changed at different HRTs; with increasing dominant species phylogenetically related to Clostridaceae.
Key words: Hydrogen fermentation, palm oil mill effluent, polydimethylsiloxane (PDMS), immobilisation.
Abbreviation
Abbreviations: GHG, Greenhouse gases; SMR, steam methane reforming; POME, palm oil mill effluent; COD, chemical oxygen demand; EVA, ethylene vinyl acetate copolymer; PMMA, polymethyl methaacrylate; PVA, polyvinyl alcohol; PDMS, polydimethylsiloxane; PCR-DGGE, polymerase chain reaction coupled with denaturing gradient gel electrophoresis; VSS, volatile suspended solid; HRT, hydraulic retention time; TSS, total suspended solids; VFA, volatile fatty acids; TCD, thermal conductivity detector; CPO, crude palm oil; PEO, polyethylene-octene; ASBR, anaerobic sequencing batch reactor.
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