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    Viability of Using Glycerin as a Co-substrate in Anaerobic Digestion of Sugarcane Stillage (Vinasse): Effect of Diversified Operational Strategies

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    Artigo de Periódico
    Date
    2019
    Author
    Lovato, Giovanna
    Batista, Lia Paula Poloni
    Preite, Marina Bernardes
    Yamashiro, Jessica N.
    Becker, Ana L. S.
    Vidal, Maria F. G.
    Pezini, Nathalia
    Albanez, Roberta
    Ratusznei, Suzana Maria
    Rodrigues, José Alberto Domingues
    xmlui.dri2xhtml.METS-1.0.item-sponsorship
    National Institutes of Health (NIH)
    FAPESP
    CAPES
    CNPq
    Metadata
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    Abstract
    Vinasse, from sugar and ethanol production, stands out as one of the most problematic agroindustry wastes due to its high chemical oxygen demand, large production volume, and recalcitrant compounds. Therefore, the viability of using glycerin as a co-substrate in vinasse anaerobic digestion was tested, to increase process efficiency and biogas productivity. The effect of feeding strategy, influent concentration, cycle length, and temperature were assessed to optimize methane production. Glycerin (1.53% v/v) proved to be a good co-substrate since it increased the overall methane production in co-digestion assays. CH4 productivity enhanced exponentially as influent concentration increased, but when temperature was increased to 35 °C, biogas production was impaired. The highest methane productivity and yield were achieved using fed-batch mode, at 30 °C and at an organic loading rate of 10.1 kg COD m−3 day−1: 139.32 mol CH4 m−3 day−1, 13.86 mol CH4 kg CODapplied, and 15.30 mol CH4 kg CODremoved. Methane was predominantly produced through the hydrogenotrophic route. In order to treat all the vinasse produced by a mid-size sugar and ethanol plant, nine reactors with 7263.4 m3 each would be needed. The energy generated by burning the biogas in boilers would reach approximately 92,000 MW h per season and could save up to US$ 240,000.00 per month in diesel oil demand. © 2019, Springer Science+Business Media, LLC, part of Springer Nature.
    1. Biomethane
    2. Energy
    3. Glycerin
    4. Kinetic model
    5. SBR
    6. Scale-up
    7. Stillage
    8. Vinasse
    9. Anaerobiosis
    10. Biofilms
    11. Biological Oxygen Demand Analysis
    12. Glycerol
    13. Hot Temperature
    14. Industrial Waste
    15. Kinetics
    16. Methane
    17. Saccharum
    18. Biogas
    19. Chemical oxygen demand
    20. Ethanol
    21. Productivity
    22. Substrates
    23. acetic acid
    24. alcohol
    25. biogas
    26. butyric acid
    27. diesel fuel
    28. glycerol
    29. hydrogen
    30. methane
    31. propionic acid
    32. sugar
    33. Kinetic modeling
    34. Vinasses
    35. activated sludge
    36. alcohol production
    37. anaerobic digestion
    38. Article
    39. biofuel production
    40. boiler
    41. chemical oxygen demand
    42. concentration (parameter)
    43. energy yield
    44. methanogenesis
    45. reactor monitoring
    46. sugarcane
    47. temperature
    48. vinasse
    49. anaerobic growth
    50. biochemical oxygen demand
    51. biofilm
    52. biosynthesis
    53. heat
    54. industrial waste
    55. kinetics
    56. metabolism
    57. Anaerobic digestion
    URI
    https://www.scopus.com/inward/record.uri?eid=2-s2.0-85067416926&doi=10.1007%2fs12010-019-02950-1&partnerID=40&md5=807ae2274edeeae77c45efbf2796360c
    https://repositorio.maua.br/handle/MAUA/1338
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