2015
DOI: 10.1016/j.biortech.2014.09.107
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Recovery of volatile fatty acids from fermentation of sewage sludge in municipal wastewater treatment plants

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Cited by 71 publications
(40 citation statements)
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“…An average VFAs concentration of 9.8 g/L was achieved from the excess sewage sludge at a yield of 0.38 gVFA/g VS added (533 mgCOD/g VS added ), which is higher than the yield reported for uncontrolled pH systems and is comparable with systems with pH control. Longo et al [18] reported a VFAs yield of 252 mg COD/g VS added for the system without any pH control and 398 mg COD/g VS added for the system with pH control at 10 using caustic soda. Moreover, the composition of VFAs produced by this iMBR is well suited for the denitrification process.…”
Section: Vfas Production Using Immersed Membrane Bioreactormentioning
confidence: 99%
See 1 more Smart Citation
“…An average VFAs concentration of 9.8 g/L was achieved from the excess sewage sludge at a yield of 0.38 gVFA/g VS added (533 mgCOD/g VS added ), which is higher than the yield reported for uncontrolled pH systems and is comparable with systems with pH control. Longo et al [18] reported a VFAs yield of 252 mg COD/g VS added for the system without any pH control and 398 mg COD/g VS added for the system with pH control at 10 using caustic soda. Moreover, the composition of VFAs produced by this iMBR is well suited for the denitrification process.…”
Section: Vfas Production Using Immersed Membrane Bioreactormentioning
confidence: 99%
“…Moreover, the mixture of VFAs can be used directly as a carbon source for the denitrification process without downstream purification demands. Many studies have tested the effectiveness of VFAs as a carbon source for the denitrification process [13][14][15][16][17][18]. In this regard, VFAs higher denitrification rates have been reported compared to methanol.…”
Section: Introductionmentioning
confidence: 99%
“…Recent studies utilised various reactor types (e.g., batch, continuous, microwave, fluidized bed and horizontal furnace), operating conditions (e.g., temperature, time, power and catalyst) and fuel (e.g., primary, digested, wet sludge and blends) for optimising pyrolytic product distribution and their quality as seen in Table 4 which summarises results from past studies. The bio-oil yield from sewage sludge pyrolysis ranges from 14-57.5 wt% [95][96][97][98][99][100][101][102][103][104][105]. Pokorna et al [105] reported a maximum bio-oil yield of 57.5 wt% with water content as low as 10 wt% when flash pyrolysis was conducted at 500 • C in a lab-scale semi-continuous reactor.…”
Section: Pyrolysismentioning
confidence: 99%
“…Furthermore, it decreases sludge production by 30% and carbon dioxide emissions by 20% . Significant cost savings can further arise when fermented sewage sludge is supplied as carbon source to accomplish the denitrification process (Mayer et al 2009;Ji & Chen, 2010;Longo et al 2015). The NOB can be inhibited by maintaining a high free ammonia (FA) concentration (FA > 1 mgNH 3 ⋅ L −1 ) or high free nitrous acid (FNA > 0.02 mgHNO 2 -N L −1 ) concentration in the biological reactor Vadivelu et al 2007;.…”
Section: Innovative Bioprocesses In the Mainstream And Sidestreammentioning
confidence: 99%
“…According to the pilot-scale results, the best parameters for the alkaline fermentation of sewage sludge, the solid-liquid separation and the via-nitrite nutrients removal were found out (Longo et al 2015). The production of SCVFA by alkaline fermentation has proved to be highly dependent on pH and temperature.…”
Section: Scena System Integrated In Conventional Treatment Of Sementioning
confidence: 99%