2013
DOI: 10.1016/j.biortech.2012.12.126
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Development of a treatment system for molasses wastewater: The effects of cation inhibition on the anaerobic degradation process

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Cited by 45 publications
(22 citation statements)
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“…2.8 g L À1 ; K + : 1.3 g L À1 ; Ca 2+ : 0.5 g L À1 ; Mg 2+ : 0.4 g L À1 ) during Phase 6 (Table S1). The concentrations of individual cations in this study are lower than those in previous reports of inhibition (Chen et al, 2008;Kugelman and Chin, 1971;Onodera et al, 2013). In addition, Kugelman and Chin (1971) described antagonism of toxicity by multiple cations with acetate feeding in a laboratory-scale digester, suggesting that cation inhibition of aceticlastic methanogens did not occur significantly in the MS-UASB reactor.…”
contrasting
confidence: 80%
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“…2.8 g L À1 ; K + : 1.3 g L À1 ; Ca 2+ : 0.5 g L À1 ; Mg 2+ : 0.4 g L À1 ) during Phase 6 (Table S1). The concentrations of individual cations in this study are lower than those in previous reports of inhibition (Chen et al, 2008;Kugelman and Chin, 1971;Onodera et al, 2013). In addition, Kugelman and Chin (1971) described antagonism of toxicity by multiple cations with acetate feeding in a laboratory-scale digester, suggesting that cation inhibition of aceticlastic methanogens did not occur significantly in the MS-UASB reactor.…”
contrasting
confidence: 80%
“…In addition, with high Ca 2+ concentration (780-1560 mgCa L À1 ), very low methanogenic activity (approximately <0.1 gCOD gVSS À1 d À1 ) with acetate was demonstrated by calcium precipitation in granules (Van Langerak et al, 2000). Onodera et al (2013) reported that the COD removal rate in a mesophilic (35°C) USSB reactor used to treat diluted molasses decreased from 37 kgCOD m À3 d À1 to 8 kgCOD m À3 d À1 with an increase in the influent cation concentration from approximately 4.0 to 14.3 g L À1 . However, a remarkable decrease in organic removal efficiency was not observed because OLR was increased with the monitoring of cation concentration to avoid the inhibition on the anaerobic degradation (Table S1) .…”
Section: Organic Removalmentioning
confidence: 99%
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“…Our research group has been developing a combined anaerobic-aerobic system consisting of a UASB and a downflow hanging sponge (DHS) as an energy-saving wastewater treatment system (Tandukar et al, 2007). DHS is an aerobic trickling filter system that uses sponge as the supporting medium (Takahashi et al, 2004), and it has been used for treating various industrial wastewaters (El-Kamah et al, 2011;Onodera et al, 2013). First, UASB removes most of the organic compounds and converts them to methane.…”
Section: Introductionmentioning
confidence: 99%
“…Anaerobic treatment (biomethanation) is widely applied for the treatment of molasses wastewater (Satyawali and Balakrishnan, 2008;Onodera et al, 2013). However, the removal of color in anaerobic treatment is not significant (Satyawali and Balakrishnan, 2008).…”
Section: Introductionmentioning
confidence: 99%