2000
DOI: 10.1385/abab:84-86:1-9:731
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Development of a Modified Three-Stage Methane Production Process Using Food Wastes

Abstract: A modified three-stage system was developed for the rapid production of methane from food wastes. The primary stage was a semianaerobic hydrolysis/acidogenic system, in which approx 4100 mg/L of volatile fatty acids (VFAs) was produced at a hydraulic retention time (HRT) of 2 d. The operation temperature and pH were 30 degrees C and 5.0-5.5, respectively. The non-degraded materials were removed through a hole at the bottom of the reactor. The secondary stage was an anaerobic acidogenic system equipped with an … Show more

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Cited by 18 publications
(4 citation statements)
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“…From the secondary reactor, output liquids and solids are transferred to a tertiary reactor where methane-rich biogas is produced. Likewise, in a two-stage system, a part, or all of the effluent from the tertiary reactor can be recirculated back to the digester depending on the targeted HRT and process efficiency [159]. According to the study by Kim et al [159], using a three-stage reactor, COD removal efficiency of over 95% was achieved for food waste AD.…”
Section: Configurationmentioning
confidence: 99%
See 1 more Smart Citation
“…From the secondary reactor, output liquids and solids are transferred to a tertiary reactor where methane-rich biogas is produced. Likewise, in a two-stage system, a part, or all of the effluent from the tertiary reactor can be recirculated back to the digester depending on the targeted HRT and process efficiency [159]. According to the study by Kim et al [159], using a three-stage reactor, COD removal efficiency of over 95% was achieved for food waste AD.…”
Section: Configurationmentioning
confidence: 99%
“…Likewise, in a two-stage system, a part, or all of the effluent from the tertiary reactor can be recirculated back to the digester depending on the targeted HRT and process efficiency [159]. According to the study by Kim et al [159], using a three-stage reactor, COD removal efficiency of over 95% was achieved for food waste AD. In a more recent study [7], an 11-23% increase in methane yield for a three-stage codigestion of food waste and horse manure was reported.…”
Section: Configurationmentioning
confidence: 99%
“…Hydrolysis reactor uses CSTR while methanogenesis reactor uses CSTR, AFB i.e., anaerobic fixed bed or USAB (de Lemos Chernicharo 2007). The acetogenesis step is carried out in a separate reactor in the three-stage system (Kim et al 2000). The basic design of the three-stage reactor is shown in Fig.…”
Section: Multi-stage Ad Processmentioning
confidence: 99%
“…One of the first studies on three-stage AD originate from Kim et al (2000). Under mesophilic conditions, FW was treated in a STR for hydrolysis/acidogenesis and two UASB for acidogenesis/ acetogenesis/methanogenesis.…”
Section: Three-stage Processesmentioning
confidence: 99%