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    Scale-up and energy estimations of single- and two-stage vinasse anaerobic digestion systems for hydrogen and methane production

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    Artigo de Periódico
    Date
    2022
    Author
    Ramos, Lucas Rodrigues
    Lovato, Giovanna
    Rodrigues, José Alberto Domingues
    Silva, Edson Luiz
    xmlui.dri2xhtml.METS-1.0.item-sponsorship
    FAPESP
    CAPES
    CNPq
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    Abstract
    This study evaluated the full-scale vinasse anaerobic digestion for industrial application. Twelve scenarios were simulated, considering single (methanogenic reactor) and two-stage systems (acidogenic + methanogenic reactors), raw and concentrated vinasse, thermophilic and mesophilic conditions for methanogenesis and usage of acidogenic or methanogenic reactor effluent to dilute vinasse. A single-stage anaerobic digestion system of 17,433 m³ necessary to treat all the raw vinasse produced by a mill with a grinding capacity of 3.3 million tons of sugarcane per season can generate a power of 11.1 MW with an energy yield of 4.6 MJ/kg CODremoved. Two-stage system scenarios where vinasse was diluted with acidogenic reactor effluent had worse energetic recoveries than the single-stage system. Nonetheless, the usage of the methanogenic reactor effluent to dilute vinasse and its own influent in a two-stage system achieved an energetic recovery at least 34% higher than that of the single-stage system. In the best two-stage scenario, the total working volume was 19,666 m³, combining thermophilic acidogenic reactors and mesophilic methanogenic reactors, with an energy yield of 7.0 MJ/kg CODremoved. The different combinations of temperatures allow for a safer and more economic operation. The proposed novel industrial configuration can be divided into two parallel acidogenic reactors of 1,800 m³ each, and those reactors are in series with eight parallel methanogenic reactors of 2,828 m³ each. The electricity produced by the full-scale system can supply an energy demand of 24 thousand inhabitants per harvest season (9.7 kWh per ton of sugarcane). This study presents a novel discussion for sugarcane industry decision makers, such as plant managers, process and project engineers, providing a trade-off between highest energy production, optimal COD removal and lowest reactor volume (CAPEX investment) that better fits their needs. © 2022 Elsevier Ltd
    1. Bioenergy recovery potential
    2. Biohythane
    3. Ethanol biorefinery
    4. Industrial reactor
    5. Reactor integration
    6. Sugarcane stillage processing
    7. Decision making
    8. Economic and social effects
    9. Effluents
    10. Investments
    11. Recovery
    12. Bio-energy
    13. Industrial reactors
    14. Methanogenic reactor
    15. Stillage
    16. Vinasses
    17. Anaerobic digestion
    URI
    https://www.scopus.com/inward/record.uri?eid=2-s2.0-85126897290&doi=10.1016%2fj.jclepro.2022.131459&partnerID=40&md5=65a313c54214225af105ec497f0487df
    https://repositorio.maua.br/handle/MAUA/1403
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