2016
DOI: 10.1016/j.watres.2015.10.055
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Augmentation of protein-derived acetic acid production by heat-alkaline-induced changes in protein structure and conformation

Abstract: a b s t r a c tWaste-derived acetic acid (HAc) is an attractive feedstock for microbe-mediated biofuel production. However, fermentative conversion of HAc from waste-activated sludge (WAS) has low yield because of the high concentration of proteins not readily utilizable by microorganisms without prior hydrolysis. We investigated a combined technology for HAc augmentation during sludge protein fermentation. The maximal HAc yield increased over two-fold, reaching 0.502 ± 0.021 g/g protein (0.36 ± 0.01 g COD/g C… Show more

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Cited by 47 publications
(8 citation statements)
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“…The sludge characteristics are similar to those presented in our previous work 34 . The collected sludge was initially filtered using a 0.45 mm mesh to remove small particles, washed twice with distilled water, and finally stored at −4 °C for further respirometry tests.…”
Section: Methodssupporting
confidence: 86%
“…The sludge characteristics are similar to those presented in our previous work 34 . The collected sludge was initially filtered using a 0.45 mm mesh to remove small particles, washed twice with distilled water, and finally stored at −4 °C for further respirometry tests.…”
Section: Methodssupporting
confidence: 86%
“…In the fed-batch reactors, the addition rate of hydrolysed blood with trypsin was much lower than that of the semi-continuous reactors; therefore, its activity reduction rate was probably higher than the amount of trypsin addition avoiding the negative effects observed in the semicontinuous reactors. Therefore, for (semi)-continuous operation, the other pre-treatment methods should be used to facilitate the rate and extent of VFA production, such as heat-alkaline pre-treatment [25] and ultraviolet pretreatment [26]. The microbial community analysis proved the importance of the Firmicutes phylum and its Clostridiales order in the transformation of proteins into VFA at high concentrations, consistent with the results of bacteria community composition analysis of digester using pig blood as substrate [5].…”
Section: Discussionsupporting
confidence: 70%
“…Sludge samples containing the seed inoculum were mixed to afford feed sludge that was then transferred into six identical 2.5-L fermentation reactors at 8.6 g/L (transferred volume = 2 L) to test different methods of fermentative pH control. The test period was at least 20-day long, a typical duration for SCFA production by anaerobic sludge fermentation (Wu et al 2010, Yuan et al 2006, and it was assumed that the degree of hydrolysis can be maximised within the first 72 h under high-pH conditions (Wang et al 2016). Consequently, during the first three days (Phase I) of the experimental process, five fermentation reactors (R1-R5) were maintained at a constant pH of 11 by addition of 2 M NaOH.…”
Section: Operation Of Sludge Fermentation Reactorsmentioning
confidence: 99%
“…Sludge and biogas samples were collected from reactors every 24 h using previously described procedures (Cai et al 2004, Wang et al 2016 and subjected to chemical analysis (for details, see Section 2.6). In addition, sludge samples collected on days 3 (Phase I end) and 25 (Phase II end) were also used to analyse microbial populations in relation to hydrolysis, acidification, and methanogenesis.…”
Section: Reactor Performance Monitoringmentioning
confidence: 99%
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