Abstract
An integrated biorefinery concept for 2nd generation bioethanol production together with biogas production from the fermentation effluent was tested in pilot-scale. The pilot plant comprised pretreatment, enzymatic hydrolysis, hexose and pentose fermentation into ethanol and anaerobic digestion of the fermentation effluent in a UASB (upflow anaerobic sludge blanket) reactor. Operation of the 770 liter UASB reactor was tested under both mesophilic (38ºC) and thermophilic (53ºC) conditions with increasing loading rates of the liquid fraction of the effluent from ethanol fermentation. At an OLR of 3.5 kg-VS/(m3•d) a methane yield of 340 L/kg-VS was achieved for thermophilic operation while 270 L/kg-VS was obtained under mesophilic conditions. Thermophilic operation was, however, less robust towards further increase of the loading rate and for loading rates higher than 5 kg-VS/(m3•d) the yield was higher for mesophilic than for thermophilic operation. The effluent from the ethanol fermentation showed no signs of toxicity to the anaerobic microorganisms. Implementation of the biogas production from the fermentation effluent accounted for about 30% higher biofuels yield in the biorefinery compared to a system with only bioethanol production.
Originalsprog | Engelsk |
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Publikationsdato | 2010 |
Antal sider | 8 |
Status | Udgivet - 2010 |
Begivenhed | 12th World Congress on Anaerobic Digestion - Guadalajara, Mexico Varighed: 31 okt. 2010 → 4 nov. 2010 |
Konference
Konference | 12th World Congress on Anaerobic Digestion |
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Land/Område | Mexico |
By | Guadalajara |
Periode | 31/10/2010 → 04/11/2010 |