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    Charge neutralization mechanism efficiency in water with high color turbidity ratio using aluminium sulfate and flocculation index

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    Charge neutralization mechanism efficiency in water with high color turbidity ratio using aluminium sulfate and flocculation index.pdf (15.40Mb)
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    Artigo de Periódico
    Date
    2020
    Author
    Cruz, Dafne
    Pimentel, Marcio
    Russo, Ana
    Cabral, Wilson
    xmlui.dri2xhtml.METS-1.0.item-sponsorship
    DCTA
    Departamento de Ciência e Tecnologia Aeroespacial
    PROAP
    CAPES
    Metadata
    Show full item record
    Abstract
    Most of the water supplied in Brazil comes from water streams that may have higher values for apparent color than turbidity. Treatability trials were performed for color and turbidity removal to evaluate the advantages of coagulation during the charge neutralization mechanism when compared to sweep flocculation for water with those characteristics. There were three types of trials: conventional Jar Test with raw water, with and without filtration, and in a pilot Water Treatment Plant, direct downward filtration, with synthetic water. Auxiliary equipment such as Continuous Flocculation Monitoring Equipment (CFME) and image analysis were used to evaluate the growth of flocs. In the Jar Tests experiments, similar levels of color (61.49%) and turbidity (61.30%) removal were observed, with a lower dosage of coagulant (46 mg/L) in the charge neutralization mechanism compared to the ones with sweep flocculation (58.22% for color and 54.73% for turbidity removal with 52 mg/L of aluminium sulfate). Similar results were found on pilot plant. At filtration rates of 180 and 300 m3 m-2 day-1, sweep flocculation mechanism had shorter filtration cycle (<5 m3) compared to other mechanisms. Therefore, a change in the operation of Water Treatment plants that use a coagulant dosage associated with sweep flocculation can bring advantages such as the reduction of coagulant consumption and sludge productions, as well as the increase of chlorine disinfection and filtration cycles. © 2020 by the authors.
    1. Apparent color
    2. Charge neutralization
    3. Coagulation mechanisms
    4. Flocculation index
    5. Treatability trials
    6. Brazil
    7. Aluminum sulfate
    8. Auxiliary equipment
    9. Chemical water treatment
    10. Coagulation
    11. Color
    12. Flocculation
    13. Ostwald ripening
    14. Pilot plants
    15. Sulfur compounds
    16. Turbidity
    17. Water filtration
    18. Water treatment plants
    19. Aluminium sulfates
    20. Chlorine disinfection
    21. Coagulation mechanism
    22. Flocculation mechanisms
    23. Monitoring equipment
    24. Turbidity removal
    25. coagulation
    26. color
    27. concentration (composition)
    28. equipment
    29. flocculation
    30. index method
    31. inorganic compound
    32. neutralization
    33. sulfate
    34. turbidity
    35. Chemicals removal (water treatment)
    URI
    https://www.scopus.com/inward/record.uri?eid=2-s2.0-85081117198&doi=10.3390%2fw12020572&partnerID=40&md5=2c5e3041d2c72a7b3374a81bc9b29271
    https://repositorio.maua.br/handle/MAUA/1349
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