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UNIT –III
1
THEORY & DESIGN OF SECONDARY TREATMENT UNITS:
 Introduction to unit operations and processes for
secondary treatment.
 Principles of biological treatments,
 important microorganisms in waste water & their
importance in waste water treatment systems,
 bacterial growth, general growth pattern, growth in
terms of bacterial numbers and bacterial mass.
 Kinetics of biological growth, cell growth, substrate
limited growth, cell growth and substrate utilization,
effect of endogenous metabolism.
UNIT OPERATIONS AND UNITPROCESSES
FOR SEWAGE TREATMENT
2
 Physical Unit Operations
 Involves physical change such as separation,
evaporation, filtration, sedimentation, adsorption,
absorption etc.
 Chemical Unit Processes
 Involves chemical reactions such as neutralization,
coagulation, etc.
 Biological Unit Processes
 ASP
 Oxidation pond
 Stabilization pond
 Biological filtration
CLASSIFICATION OF
SEWAGE TREATMENT
3
 Preliminary Treatment
 Primary Treatment
 Secondary Treatment
 Tertiary Treatment
BIOLOGICAL PRINCIPAL
4
 Under proper environment condition, the soluble
organic substances of the waste are completely
destroyed by biological oxidation.
 The end products of the metabolism are either
gas or liquid.
BIOLOGICAL
UNIT PROCESSES
 Classification of biological treatment:
 Aerobic processes
 Anaerobic processes
 Anoxic processes
 Facultative processes
Further subdivided:
 Suspended growth processes
 Attached growth processes
 Combined growth processes 6
MICROORGANISM IN ACTIVATED SLUDGE PROCESS
Create a very rich environment
for growth of a diverse
microbial community
MICROOROGANISMS IN TRICKLING FILTER
BACTERIALGROWTH
8
 Log and exponential growth phase
 Declining or retarded growth phase
 Endogenous growth phase or death phase
OXYGEN REQUIREMENT IN AEROBIC PROCESSES
9
 Oxygen requirement will be equal to the amount
that would be required to remove all the BOD by
oxidation for the fraction of BOD removed by
sludge wasting.
C5H7NO2 + 5O2 5CO2+2H2O+NH3
113(Cells) 5(32)
kg O2/kg cells= 160/113=1.42
Therefore ,
BOD of cells=1.42(mass of cells)
 Theoretical oxygen requirement-
kg O2/day=(total mass of BOD
utilized
10
kg/day-1.42(mass of organisms wasted,
kg/day)
Kg O2/day =Q(SO-S)/F-1.42(QWXR)
XR=micro-organism conc. in the waste.
F=conversion factor for converting BOD5 to
BODL=(1/1.470)=0.68
This allows only for carbonaceous BOD removal.
TREATMENTS
11
 Activated sludge processes
 Trickling filter process
ACTIVATED SLUDGE PROCESSES
12
 Activated sludge- is the sludge which is obtained
by settling sewage in presence of abundant
oxygen.
 RESULT=
 OM present in sewage is oxidised
 Suspended and colloidal matter coagulate and
form flocculent masses which are readily
settleble.
WORKING
13
 The organism oxidize a portion of the OM present
in the sewage to CO2 and H2O and other end
products and energy
 Synthesize the other portion OM and convert into
new microbial cell tissue using energy.
 Endogenous respiration.
OPERATION AND UNITS
14
 Mixing regime.
 Plug flow.
 Completely mixed flow.
 Flow scheme
METHODS OF AERATION
15
 Diffused air aeration
 Mechanical aeration
 Combined aeration
LOADING RATE OF AERATION TANK
16
 Hydraulic retention time.
 Volumetric BOD loading.
 Food to micro-organism ratio.
 Mean cell residence time.
SLUDGE PRODUCTION AND PROCESS CONTROL
17
 Rate of sludge production.
 Sludge volume index.
TYPES OF ACTIVATED SLUDGE PROCESSES
18
 Conventional Activated sludge processes
 Tapered aeration process
 Step aeration process
OPERATIONAL DIFFICULTIES
19
 Rising sludge
 Bulking of sludge
 Advantages
o Clear sparkling effluent of high quality.
o Process requires small area of land.
o There is freedom from fly and odour nuisance.
o Process is highly efficient. Removal of SS,BOD
and bacteria around 90% each.
o Low cost of installation than trickling filters.
20
 Disadvantages
o If there is sudden increase in the quantity of
sewage, effluent of poor quality is obtained.
o Operation cost of the process is high.
o Large quantity of wet sludge is obtained at the
end process.
21
THANK YOU
28

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CLASSIFICATION OF SEWAGE TREATMENT

  • 1. UNIT –III 1 THEORY & DESIGN OF SECONDARY TREATMENT UNITS:  Introduction to unit operations and processes for secondary treatment.  Principles of biological treatments,  important microorganisms in waste water & their importance in waste water treatment systems,  bacterial growth, general growth pattern, growth in terms of bacterial numbers and bacterial mass.  Kinetics of biological growth, cell growth, substrate limited growth, cell growth and substrate utilization, effect of endogenous metabolism.
  • 2. UNIT OPERATIONS AND UNITPROCESSES FOR SEWAGE TREATMENT 2  Physical Unit Operations  Involves physical change such as separation, evaporation, filtration, sedimentation, adsorption, absorption etc.  Chemical Unit Processes  Involves chemical reactions such as neutralization, coagulation, etc.  Biological Unit Processes  ASP  Oxidation pond  Stabilization pond  Biological filtration
  • 3. CLASSIFICATION OF SEWAGE TREATMENT 3  Preliminary Treatment  Primary Treatment  Secondary Treatment  Tertiary Treatment
  • 4. BIOLOGICAL PRINCIPAL 4  Under proper environment condition, the soluble organic substances of the waste are completely destroyed by biological oxidation.  The end products of the metabolism are either gas or liquid.
  • 5. BIOLOGICAL UNIT PROCESSES  Classification of biological treatment:  Aerobic processes  Anaerobic processes  Anoxic processes  Facultative processes Further subdivided:  Suspended growth processes  Attached growth processes  Combined growth processes 6
  • 6. MICROORGANISM IN ACTIVATED SLUDGE PROCESS Create a very rich environment for growth of a diverse microbial community
  • 8. BACTERIALGROWTH 8  Log and exponential growth phase  Declining or retarded growth phase  Endogenous growth phase or death phase
  • 9. OXYGEN REQUIREMENT IN AEROBIC PROCESSES 9  Oxygen requirement will be equal to the amount that would be required to remove all the BOD by oxidation for the fraction of BOD removed by sludge wasting. C5H7NO2 + 5O2 5CO2+2H2O+NH3 113(Cells) 5(32) kg O2/kg cells= 160/113=1.42 Therefore , BOD of cells=1.42(mass of cells)
  • 10.  Theoretical oxygen requirement- kg O2/day=(total mass of BOD utilized 10 kg/day-1.42(mass of organisms wasted, kg/day) Kg O2/day =Q(SO-S)/F-1.42(QWXR) XR=micro-organism conc. in the waste. F=conversion factor for converting BOD5 to BODL=(1/1.470)=0.68 This allows only for carbonaceous BOD removal.
  • 11. TREATMENTS 11  Activated sludge processes  Trickling filter process
  • 12. ACTIVATED SLUDGE PROCESSES 12  Activated sludge- is the sludge which is obtained by settling sewage in presence of abundant oxygen.  RESULT=  OM present in sewage is oxidised  Suspended and colloidal matter coagulate and form flocculent masses which are readily settleble.
  • 13. WORKING 13  The organism oxidize a portion of the OM present in the sewage to CO2 and H2O and other end products and energy  Synthesize the other portion OM and convert into new microbial cell tissue using energy.  Endogenous respiration.
  • 14. OPERATION AND UNITS 14  Mixing regime.  Plug flow.  Completely mixed flow.  Flow scheme
  • 15. METHODS OF AERATION 15  Diffused air aeration  Mechanical aeration  Combined aeration
  • 16. LOADING RATE OF AERATION TANK 16  Hydraulic retention time.  Volumetric BOD loading.  Food to micro-organism ratio.  Mean cell residence time.
  • 17. SLUDGE PRODUCTION AND PROCESS CONTROL 17  Rate of sludge production.  Sludge volume index.
  • 18. TYPES OF ACTIVATED SLUDGE PROCESSES 18  Conventional Activated sludge processes  Tapered aeration process  Step aeration process
  • 19. OPERATIONAL DIFFICULTIES 19  Rising sludge  Bulking of sludge
  • 20.  Advantages o Clear sparkling effluent of high quality. o Process requires small area of land. o There is freedom from fly and odour nuisance. o Process is highly efficient. Removal of SS,BOD and bacteria around 90% each. o Low cost of installation than trickling filters. 20
  • 21.  Disadvantages o If there is sudden increase in the quantity of sewage, effluent of poor quality is obtained. o Operation cost of the process is high. o Large quantity of wet sludge is obtained at the end process. 21