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Improving the energy balance of ethanol industry with methane production from vinasse and molasses in two-stage anaerobic reactors
Thermophilic anaerobic digestion is a viable option for processing sugarcane vinasse that recovers energy in the form of methane. However, restarting real-scale vinasse-treating reactors, at the resumption of the sugarcane harvest season, can lead to difficulties, making it desirable to keep them in...
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Published in: | Journal of cleaner production 2019-11, Vol.238, p.117577, Article 117577 |
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Main Authors: | , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | Thermophilic anaerobic digestion is a viable option for processing sugarcane vinasse that recovers energy in the form of methane. However, restarting real-scale vinasse-treating reactors, at the resumption of the sugarcane harvest season, can lead to difficulties, making it desirable to keep them in continuous operation in the off-season. Thus, was evaluated the thermophilic anaerobic conversion of sugarcane vinasse in a two-stage upflow anaerobic sludge blanket (UASB) reactor (reactors R1 and R2), employing sugarcane molasses in the off-season for methane production, followed again by vinasse in the following harvest season. UASB reactor R2 yielded a higher methane percentage in biogas and higher volumetric methane production rates and methane yield than R1, accounting for a 58% increase in energy production in the two-stage system compared to the single-stage system using vinasse. It is observed that the molasses is an important source of carbon for the energy production using the thermophilic UASB reactors (18.01 MJ L−1 molasses), compared to alcoholic fermentation (8.30 MJ L−1 molasses). The methane produced in the reactors system (R1 + R2), after the off-season, can generate 5.1 kWh d−1 per m3 of vinasse, or 17% of the electricity needed to process a ton of sugarcane.
Anaerobic reactors can remain in operation with molasses during sugarcane harvestAnaerobic system yielded of 0.275 m3 CH4 kg−1 of removed chemical organic demandEnergy production for the two-stage system was 58% higher than for the single-stageEnergy recovered from molasses by the reactors is higher, compared to ethanol production. |
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ISSN: | 0959-6526 1879-1786 |
DOI: | 10.1016/j.jclepro.2019.07.052 |