Author/Authors :
Wang، نويسنده , , Zhen-zhong Lv، نويسنده , , Zhe and Du، نويسنده , , Jiliang and Mo، نويسنده , , Chunling and Yang، نويسنده , , Xiushan and Tian، نويسنده , , Shen، نويسنده ,
Abstract :
A combined process was designed for the co-production of ethanol and methane from unwashed steam-exploded corn stover. A terminal ethanol titer of 69.8 g/kg mass weight (72.5%) was achieved when the fed-batch mode was performed at a final solids loading of 35.5% (w/w) dry matter (DM) content. The whole stillage from high-solids ethanol fermentation was directly transferred in a 3-L anaerobic digester. During 52-day single-stage digester operation, the methane productivity was 320 mL CH4/g volatile solids (VS) with a maximum VS reduction efficiency of 55.3%. The calculated overall product yield was 197 g ethanol + 96 g methane/kg corn stover. This indicated that the combined process was able to improve overall content utilization and extract a greater yield of lignocellulosic biomass compared to ethanol fermentation alone.
Keywords :
High solids fed batch SSF , Anaerobic digestion , mass balance , Ethanol and methane co-production