The role of phase separation and feed cycle length in leach beds coupled to methanogenic reactors for digestion of a solid substrate (Part 1): Optimisation of reactors' performance.
A two-phase system composed by a leach bed and a methanogenic reactor was modified for the first time to improve volumetric substrate degradation and methane yields from a complex substrate (maize; Zeamays). The system, which was operated for consecutive feed cycles of different durations for 120 days, was highly flexible and its performance improved by altering operational conditions. Daily substrate degradation was higher the shorter the feed cycle, reaching 8.5 g TSdestroyed d(-1) (7-day feed cycle) but the overall substrate degradation was higher by up to 55% when longer feed cycles (14 and 28 days) were applied. The same occurred with volumetric methane yields, reaching 0.839 m3 (m3)(-1) d(-1). The system performed better than others on specific methane yields, reaching 0.434 m3 kg(-1) TSadded, in the 14-day and 28-day systems. The UASB and AF designs performed similarly as second stage reactors on methane yields, SCOD and VFA removal efficiencies.
University of Southampton, School of Civil Engineering and the Environment, University Road, Southampton SO17 1BJ, UK. denisecysneiros@hotmail.com
Denise
D
Cysneiros
Charles J
CJ
Banks
Sonia
S
Heaven
Kimon-Andreas G
KA
Karatzas
D061249:Batch Cell Culture Techniques / Q000295:instrumentation* / Q000592:standards*; D057919:Biological Oxygen Demand Analysis; D019149:Bioreactors; D005232:Fatty Acids, Volatile / Q000032:analysis; D006863:Hydrogen-Ion Concentration; D008697:Methane / Q000032:analysis*; D012037:Refuse Disposal / Q000295:instrumentation* / Q000379:methods*; D003313:Zea mays / Q000378:metabolism*
D005232:Fatty Acids, Volatile; D008697:Methane