2007
DOI: 10.1016/j.procbio.2006.07.013
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The energy balance in farm scale anaerobic digestion of crop residues at 11–37°C

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Cited by 60 publications
(17 citation statements)
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“…The effluent in this study was produced with an organic loading rate and water dilution rate expected to give a lactate and volatile fatty acid (VFA) concentration of less than 0.2 g dm -3 . This concentration is somewhat higher than that measured in the same reactor in other years, but is consistent with values reported by Zauner and Küntzel (1986) for biodigestion of grass/clover and by Bohn et al (2007) for biodigestion of sugar beet leaves. According to extrapolation from linear-regression equations presented by Kirchmann and Lundvall (1993), N immobilization due to application of such a biogas effluent with a VFA level of 0.2 g dm -3 should be less than 9 mg N pot -1 for the higher (150 N) fertilization level and should be soon remineralized.…”
Section: First Six-week Periodsupporting
confidence: 91%
“…The effluent in this study was produced with an organic loading rate and water dilution rate expected to give a lactate and volatile fatty acid (VFA) concentration of less than 0.2 g dm -3 . This concentration is somewhat higher than that measured in the same reactor in other years, but is consistent with values reported by Zauner and Küntzel (1986) for biodigestion of grass/clover and by Bohn et al (2007) for biodigestion of sugar beet leaves. According to extrapolation from linear-regression equations presented by Kirchmann and Lundvall (1993), N immobilization due to application of such a biogas effluent with a VFA level of 0.2 g dm -3 should be less than 9 mg N pot -1 for the higher (150 N) fertilization level and should be soon remineralized.…”
Section: First Six-week Periodsupporting
confidence: 91%
“…Anaerobic digestion has now become a commonly applied biological process for stabilization of sewage sludges (Arnaiz et al 2006;Aitken et al 2005). The process is more beneficial among several sludge stabilization methods by reason of it having be able to produce a net energy gain (Mao et al 2004;Bohn et al 2007) in the form of methane gas leading to cost-effectiveness (Mao et al 2004). The biodegradability of waste sludge can be improved by using thermal energy (Bougrier et al 2008), enzymes and bacteria ), ozonation (Zhang et al 2009;Dytczak et al 2007), acidification, alkaline addition (López Torres and Espinosa Lloréns 2008), high pressure homogenization (Kidak et al 2009), mechanical disintegration and ultrasound (Chu et al 2001) pre-treatments.…”
Section: Sludge Digestionmentioning
confidence: 99%
“…Psychrophilic temperatures can be used for small-scale digesters without heating. However, biogas production at psychrophil temperature is much slower compared to at higher that temperature conditions (Collins et al 2006;Bohn et al 2007;Hesselgren et al 2005). The large-scale anaerobic digesters in Europe are mostly run at mesophilic or thermophilic conditions (Table 6.3).…”
Section: Temperaturementioning
confidence: 99%