2017
DOI: 10.1016/j.ijhydene.2017.07.178
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Pretreatment conditions of palm oil mill effluent (POME) for thermophilic biohydrogen production by mixed culture

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Cited by 61 publications
(19 citation statements)
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“…For process intensification, the approaches such as pure culture, continuous operation, consolidated saccharification and fermentation, chemical additions, are optimization avenues. In this work, for convenience of discussions, the comparisons were divided into the following five categories, namely pure culture (PC) [73,[84][85][86][87][88][89][90][91][92][93][94], chemical additions (CA) [2,39,76,[95][96][97], continuous operation with mixed culture (COMC) [98][99][100][101][102], batch operation with mixed culture (BOMC) [103][104][105][106][107][108] and consolidated saccharification and fermentation (CSF) [18,31,61,[109][110][111], respectively. For quantitative comparison of hydrogen yield across different literatures, the necessary Carbon-molar-based mass balance for DF is pivotal and necessary.…”
Section: Results Comparison Among Different Process Intensificationsmentioning
confidence: 99%
“…For process intensification, the approaches such as pure culture, continuous operation, consolidated saccharification and fermentation, chemical additions, are optimization avenues. In this work, for convenience of discussions, the comparisons were divided into the following five categories, namely pure culture (PC) [73,[84][85][86][87][88][89][90][91][92][93][94], chemical additions (CA) [2,39,76,[95][96][97], continuous operation with mixed culture (COMC) [98][99][100][101][102], batch operation with mixed culture (BOMC) [103][104][105][106][107][108] and consolidated saccharification and fermentation (CSF) [18,31,61,[109][110][111], respectively. For quantitative comparison of hydrogen yield across different literatures, the necessary Carbon-molar-based mass balance for DF is pivotal and necessary.…”
Section: Results Comparison Among Different Process Intensificationsmentioning
confidence: 99%
“…Hydrogenic POME effluent was obtained from the BioH 2 fermentation reactor fed with pre-treated POME (dilute nitric acid pre-treatment) 71 . The hydrogenic POME effluent was of brown-yellowish colour with a strong sour smell at the pH between 4.8 and 5.2, temperature of 55 °C, total COD of 63.27 ± 5.2 g/L, VFA of 3.25 ± 0.75 g CaCO 3 /L, TSS of 17.5 ± 2.0 g/L and VSS of 8.85 ± 1.5 g/L.…”
Section: Methodsmentioning
confidence: 99%
“…*The total sugar consumed as glucose equivalent. **Pre-treated POME with dilute nitric acid71 . ***Biohydrogen production in the first-stage anaerobic fermentation28 .…”
mentioning
confidence: 99%
“…Numerous technologies have been investigated in the last decade to reduce the environmental risks from the palm oil biodiesel industry, as addressed by Abdul-Hamid et al [20]. Traditional ponding system has been the preferred technique to treat palm oil mill effluent [21], but this method has some limitations, such as higher greenhouse gas (GHG) emissions. One of the solutions is proposed by Jamaludin et al [22] to use recycling water to reduce GHG emissions.…”
Section: Challenges With Indonesian and Malaysian Palm Oil-biodiesel Industrymentioning
confidence: 99%