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Am I Surface Water Scientist ?
   Specific to Hydrology, water shed,
    pollution but not limnology
   Skill towards Environmental
    Innovations & contribution to this
    emerging science
   Water quality to aquatic life,
    agricultural use and recreation &
    aesthetic purpose
Aerobic Submerged
  Attached Growth
Bioreactor: A Suitable
Device for Intermediary
Wastewater Treatment
Specific Objectives:

   To assess the organic matter degradation
    efficiency under different solids and
    salinity proportions in wastewater.
   To evaluate ammonia nitrogen removal
    capability under submerged condition of
    bioreactor.
   To find out relation between bacterial
    intensity and the degree of waste removal.
Experimental setup for the different
    particle size experiments
Experimental setup for the material
    comparison experiments
: Initial conditions of MCE (stone,
         glass & tire) experiment
                                 Experiment-1 Experiment-2 Experiment-3


COD (mg/L)                       2275         2190         4465
BOD (mg/L)                       330          760          1506
NH3-N (mg/L)                     302          1000         1730
Packed bed depth (cm)            75           90           90
Bacterial Density (cfu/ml)       2.3 * 104    19.2 * 104   300 * 104
Total solids (mg/L)              2400         10400        15200
Total suspended solids (mg/L) 26              200          985
Electrical       Conductivity 6060            9500         13500
(µS/m)
Hydraulic loading (m3 m-2 d-1)   2.0          4.0          4.0
Measuring parameters and instruments
Measured parameters       Measuring instruments

Dissolved oxygen          DO meter of model OM-51
Chemical oxygen           COD vial and Lambda 20 Spectrometer
demand
Ammonia-nitrogen          NH3-N electrode (5002-10C) with multi-meter
                          model D-53
Total dissolved solid     Oven
Total Suspended solid     Vacuum extractor and Oven
Electrical conductivity   Conductivity meter of model ES-51
pH                        pH electrode (6066-10C) with multi-meter
Biomass weight            Electronic balance
Bio-film thickness        Digital caliper
Air flow supply           Aerator
Wastewater flow supply Small submergible pump
Sample of prepared agar for
   culturing bacteria
CFU sample collection
Bio-oxidation of organic matters in recirculation process
Nitrification trends in recirculation process
Bacterial performance in recirculation process
Overall performance in Third Cycle experiments


             COD%    BOD%    NH3-N%   HC%      TS%     CFU 104   EC
Initial
value        4465    1506    1730     150      15200   300       13500
Mixed tire   53.95   97.17   95.53    47.02    15.30
Large tire   52.86   98.41   85.01    31.90    17.43
Medium
tire         56.67   97.79   79.17    29.37    18.91
Small tire   55.04   99.12   90.34    40.87    15.63
Crumb tire   52.31   98.50   75.44    100.00   13.65
Mean         54.63   98.12   87.51    37.29    16.82
STDEV        1.6     0.8     7.0      8.2      1.7
Stone        55.3    97.6    96.8              22.4
Glass        55.0    98.7    93.1              22.6
Tire         55.6    98.6    81.3              23.8
Mean         55.31   98.29   90.39             22.97
Conclusion
   Aerobic submerged bioreactor has
    been proved to be a potential device
    for secondary treatment of
    wastewater.
   The rate of remediation of
    wastewater depends on the intensity
    of bacterial growth.
   High salinity retards the remediation
    process i.e. the bacterial growth.
Conclusion
   The experimental results indicate
    that spherical shaped. i.e. the small
    size tire chips are better for bio-
    remediation for landfill leachate
    treatment than rectangular shape.
   In submergence bioreactor clogging
    rate is slower than trickling filter
    and clogging can be eliminated
    through backwashing .

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Bioreactor Design

  • 1. Am I Surface Water Scientist ?  Specific to Hydrology, water shed, pollution but not limnology  Skill towards Environmental Innovations & contribution to this emerging science  Water quality to aquatic life, agricultural use and recreation & aesthetic purpose
  • 2. Aerobic Submerged Attached Growth Bioreactor: A Suitable Device for Intermediary Wastewater Treatment
  • 3. Specific Objectives:  To assess the organic matter degradation efficiency under different solids and salinity proportions in wastewater.  To evaluate ammonia nitrogen removal capability under submerged condition of bioreactor.  To find out relation between bacterial intensity and the degree of waste removal.
  • 4. Experimental setup for the different particle size experiments
  • 5. Experimental setup for the material comparison experiments
  • 6. : Initial conditions of MCE (stone, glass & tire) experiment Experiment-1 Experiment-2 Experiment-3 COD (mg/L) 2275 2190 4465 BOD (mg/L) 330 760 1506 NH3-N (mg/L) 302 1000 1730 Packed bed depth (cm) 75 90 90 Bacterial Density (cfu/ml) 2.3 * 104 19.2 * 104 300 * 104 Total solids (mg/L) 2400 10400 15200 Total suspended solids (mg/L) 26 200 985 Electrical Conductivity 6060 9500 13500 (µS/m) Hydraulic loading (m3 m-2 d-1) 2.0 4.0 4.0
  • 7. Measuring parameters and instruments Measured parameters Measuring instruments Dissolved oxygen DO meter of model OM-51 Chemical oxygen COD vial and Lambda 20 Spectrometer demand Ammonia-nitrogen NH3-N electrode (5002-10C) with multi-meter model D-53 Total dissolved solid Oven Total Suspended solid Vacuum extractor and Oven Electrical conductivity Conductivity meter of model ES-51 pH pH electrode (6066-10C) with multi-meter Biomass weight Electronic balance Bio-film thickness Digital caliper Air flow supply Aerator Wastewater flow supply Small submergible pump
  • 8. Sample of prepared agar for culturing bacteria
  • 10. Bio-oxidation of organic matters in recirculation process
  • 11.
  • 12. Nitrification trends in recirculation process
  • 13. Bacterial performance in recirculation process
  • 14.
  • 15.
  • 16. Overall performance in Third Cycle experiments COD% BOD% NH3-N% HC% TS% CFU 104 EC Initial value 4465 1506 1730 150 15200 300 13500 Mixed tire 53.95 97.17 95.53 47.02 15.30 Large tire 52.86 98.41 85.01 31.90 17.43 Medium tire 56.67 97.79 79.17 29.37 18.91 Small tire 55.04 99.12 90.34 40.87 15.63 Crumb tire 52.31 98.50 75.44 100.00 13.65 Mean 54.63 98.12 87.51 37.29 16.82 STDEV 1.6 0.8 7.0 8.2 1.7 Stone 55.3 97.6 96.8 22.4 Glass 55.0 98.7 93.1 22.6 Tire 55.6 98.6 81.3 23.8 Mean 55.31 98.29 90.39 22.97
  • 17.
  • 18.
  • 19.
  • 20.
  • 21.
  • 22.
  • 23.
  • 24.
  • 25. Conclusion  Aerobic submerged bioreactor has been proved to be a potential device for secondary treatment of wastewater.  The rate of remediation of wastewater depends on the intensity of bacterial growth.  High salinity retards the remediation process i.e. the bacterial growth.
  • 26. Conclusion  The experimental results indicate that spherical shaped. i.e. the small size tire chips are better for bio- remediation for landfill leachate treatment than rectangular shape.  In submergence bioreactor clogging rate is slower than trickling filter and clogging can be eliminated through backwashing .

Notes de l'éditeur

  1. Slide1