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(COMMON EFFLUENT TREATMENT PLANT )
Department
School of chemical Engineering and Physical Sciences
Phagwara Punjab
Presented by
Name : SHIVPOOJAN SINGH , KRISHNANAND KUSHWAHA
Redg no. : 11615981,11607059
Section : G1606
Presented to
School of Chemical Engineering
and physical sciences
BHARUCH ENVIRO INFRASTRUCTURE LIMITED
CONTENT
1. About
2. Pipeline network
3. Introduction.
4. Parameters
5. Tanks used
6. Mechanical instruments
7. Bio-augumentation
8. Chemical preparation
9. Flow Chart :
1. Category-1
2. Category-2
3. Category-3
4. Category-4
10. Formulae
11. Sludge
12. Sludge dewatering
13. Lab tests
14. Conclusion
ABOUT
Effluent treatment plant need land for construction, capital cost, power and specialized manpower
for their operation and maintenance. Because of these constraints, small scale tanneries cannot
afford to have their own effluent treatment facilities and therefore combined effluent from all
tanneries are to be brought to a centralized place for treatment. This facility is called a Common
Effluent Treatment Plant (CETP).
Common Effluent Treatment Plant (CETP) in Baddi is an industrial waste water treatment
plant. It was established in 2013 and it is one of the largest waste water treatment plant in India. The
total cost to setup this plant was 60.95 crore rupees. It takes influent from more than 300 industries
through pipe line (62km network in Baddi) and by tankers (about 40-50 tankers/day of 20KL each) in
Baddi. CETP treats the 25 million liter of industrial waste water per day.
PIPELINE NETWORK
INTRODUCTION
CETP Baddi treats industrial waste water which comes through pipeline and
tankers. They take waste water from some industries like food, paper, textile,
soap, detergent, pharmaceutical, dye and electroplating industries. They
categories waste water of these industries according to their contamination and
they treat waste water according to that. They categories waste water in 5
different categories. They are:
 Food , paper and textile effluent
 Soap and Detergent effluent
 Pharmaceutical effluent
 Concentrated dye effluent
 Electroplating effluent
1. Biological Oxygen Demand (BOD)
2. Chemical Oxygen Demand (COD)
3. Total Suspended Solid (TSS)
4. Total Dissolved Solid (TDS)
5. Dissolved Oxygen (DO)
6. Sludge settling volume (SSV)
7. Mixed liquid suspended solid (MLSS)
8. Mixed liquid volatile suspended solid (MLVSS)
9. Potential of Hydrogen (PH)
10. Temperature (T)
MAIN PARAMETERS OF THE COMPANY
TANKS USED
• Inlet channel
• Bar screen
• Course screen
• Equalization tank
• Pre-settler
• Aeration tank
• Secondary clarifier
• Reaction tank
• Tertiary clarifier
• Tube settler
• Thickener
• Sludge sump
MECHANICAL INSTRUMENTS USED
• Pumps
• Blowers
• Rota meter
• Agitators
• Decenter
• Rack arm
BIO-AUGUMANTATION
• It is a process of making new culture (Bacteria).
Nutrition broth + media = fresh culture
Fresh Culture + Water + jaggery New Culture
(for aeration tank)
air
CHEMICAL PREPARATION
For the dosing of chemicals in reaction tank and decenter we need to prepare the
chemicals according to the demand of the effluent.
1. Poly electrolyte(anionic).
2. Poly electrolyte(cationic).
3. Poly aluminium chloride(PAC).
Poly electrolyte(anionic).
10000 L of water + 1kg of poly electrolyte powder = poly electrolyte(anionic) solution.
• Poly electrolyte(cationic).
10000 L of water + 1kg of poly electrolyte powder = poly electrolyte(cationic) solution
Poly aluminum chloride.
9500 L of water + 500 L of concentrated PAC = poly aluminium chloride solution.
CH-16
CH-1
TERTIARY
CLARIFIER-1
TERTIARY
CLARIFIER-1
PAC PE
INFFLUENT
INLET
BAR
SCREEN
COURSE
SCREEN
GREASE &
OIL
CHAMBER
EQUALIZATION TANK AIR
PRE
SETTLER
UREA, DAP & BIOMASS
SECONDRY
CLARIFIER
REACTION TANK
AEREATIONTANK
FINAL OUTLET
INLET
FROM
CH-16
AIR
60% RECIRCULATION OF FRESH
CULTURE
DAP:- Di-ammonium
Phosphate
PAC:-Poly Aluminum
Chloride
PE:- Poly
electrolyte(anionic)
SC-1:- secondary
clarifier
CSS- Chemical Sludge
Sump
THK- Thickener
To
SC-1
CATEGORY-1
THK
CSS
CSS
PAC PE
INFFLUENT
INLET
BAR
SCREEN
COURSE
SCREEN
OIL &
GREASE
CHAMBER
EQUALIZATION
TANK
SECONDRY
CLARIFIER
CAT-2
AEREATION
TANK
CAT-2
PRIMARY
TUBE
SETTLER
CH-16
REACTION
TANK-1
UREA, DAP & FRESH CULTURE
PAC PE
REACTION
TANK-2
PE PAC
TERTIARY
TUBE
SETTLER
AEREATION TANK CAT-1
CH-1
UREA, DAP & MOLASSES
`
AIR
SECONDRY
CLARIFIER
CAT-1
REACTION TANK
TERTIARY
CLARIFIER-1
TERTIARY
CLARIFIER-2
FINALOUTLET
60% RECIRCULATION OF
BIOMASS
CATEGORY-2
CSS
CSS
CSS
TO THK
TO THK
CSS
TERTIARY
CLARIFIER-1
TERTIARY
CLARIFIER-1
PAC PE
INFFLUENT
INLET
BAR
SCREEN
COURSE
SCREEN
GREASE &
OIL
CHAMBER
EQUALIZATION TANK AIR
PRE
SETTLER
UREA, DAP & FRESH CULTURE
SECONDRY
CLARIFIER
REACTION TANK
AEREATIONTANK
FINAL OUTLET
CH-1
CH-8
INLET
FROM
CH-8
AIR
60% RECIRCULATION OF BIOMASS
DAP- Di-ammonium
Phosphate
PAC-Poly Aluminum
Chloride
PE- Poly
electrolyte(anionic)
CSS- Chemical
Sludge Sump
CATEGORY-3
CSS
SETTLED SLUDGE TO THICKNER
EFFLUENT
INLET
BAR
SCREEN
COURSE
SCREEN
GREASE &
OIL
CHAMBER
EQUALIZATION TANK AIR
REACTION
TANK-I
TUBE
SETTELER
REACTION
TANK-II
FINAL OUTLET
BLEACHING
POWDER
LIME
CSS
CATEGORY-4
HClPE
1.
F/M =
BOD×INFLUENT FLOW RATE
MLVSS×AERATION TANK VOLUME
Where,
F = Food
M = Microorganism
MLVSS = Mixed Liquor Volatile Suspended Solids
BOD = Biological Oxygen Demand
2.
Treatment Charges = [0.02*So+0.03*(C-2.5*So) + 0.005*CSS+0.01*(C1- 2100)] x 1.10*[1 + R/100] y, Rs /KL
Where,
So = BOD of sample, mgs/L
C = COD of sample, mgs/L
Css = Suspended solids of sample, mgs/L
C1 = TDS of sample, mgs/L
R = Appreciation in each year.
y = no. of years from base year 2011
FORMULAE
SLUDGE
Sludge is a semi-solid slurry and can be produced as sludge from wastewater
treatment processes or as a settled suspension obtained from
conventional drinking water treatment and numerous other industrial processes.
There are two types of sludge.
1. Chemical sludge.
2. Bio-chemical sludge.
SLUDGE DEWATERING
Sludge dewatering is the separation of liquid and solid phase.
For The Dewatering Of Sludge We Use Centrifuge/decenter.
LAB TEST
1. Determination of chemical oxygen demand.
2. Determination of bio-chemical oxygen demand.
3. Determination of total suspended solid.
4. Determination of total dissolved solid.
5. Determination of pH.
6. Determination of dissolved oxygen.
CONCLUSION
Since the setting up of the CETP is a step towards reducing environmental
pollution. and we know that Baddi is known as the hub of pharmaceutical
industries in Asia. More industries at a particular place produces more effluent
because of that nearby areas get more polluted. In such areas effluent treatment
plant plays a vital role in protecting environment. According to my opinion in every
industrial estate there must be a compulsory effluent treatment plant.
ANY QUESTION
?
THANK YOU

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common effluent treatment plant

  • 1. (COMMON EFFLUENT TREATMENT PLANT ) Department School of chemical Engineering and Physical Sciences Phagwara Punjab Presented by Name : SHIVPOOJAN SINGH , KRISHNANAND KUSHWAHA Redg no. : 11615981,11607059 Section : G1606 Presented to School of Chemical Engineering and physical sciences BHARUCH ENVIRO INFRASTRUCTURE LIMITED
  • 2. CONTENT 1. About 2. Pipeline network 3. Introduction. 4. Parameters 5. Tanks used 6. Mechanical instruments 7. Bio-augumentation 8. Chemical preparation 9. Flow Chart : 1. Category-1 2. Category-2 3. Category-3 4. Category-4 10. Formulae 11. Sludge 12. Sludge dewatering 13. Lab tests 14. Conclusion
  • 3. ABOUT Effluent treatment plant need land for construction, capital cost, power and specialized manpower for their operation and maintenance. Because of these constraints, small scale tanneries cannot afford to have their own effluent treatment facilities and therefore combined effluent from all tanneries are to be brought to a centralized place for treatment. This facility is called a Common Effluent Treatment Plant (CETP). Common Effluent Treatment Plant (CETP) in Baddi is an industrial waste water treatment plant. It was established in 2013 and it is one of the largest waste water treatment plant in India. The total cost to setup this plant was 60.95 crore rupees. It takes influent from more than 300 industries through pipe line (62km network in Baddi) and by tankers (about 40-50 tankers/day of 20KL each) in Baddi. CETP treats the 25 million liter of industrial waste water per day.
  • 5. INTRODUCTION CETP Baddi treats industrial waste water which comes through pipeline and tankers. They take waste water from some industries like food, paper, textile, soap, detergent, pharmaceutical, dye and electroplating industries. They categories waste water of these industries according to their contamination and they treat waste water according to that. They categories waste water in 5 different categories. They are:  Food , paper and textile effluent  Soap and Detergent effluent  Pharmaceutical effluent  Concentrated dye effluent  Electroplating effluent
  • 6. 1. Biological Oxygen Demand (BOD) 2. Chemical Oxygen Demand (COD) 3. Total Suspended Solid (TSS) 4. Total Dissolved Solid (TDS) 5. Dissolved Oxygen (DO) 6. Sludge settling volume (SSV) 7. Mixed liquid suspended solid (MLSS) 8. Mixed liquid volatile suspended solid (MLVSS) 9. Potential of Hydrogen (PH) 10. Temperature (T) MAIN PARAMETERS OF THE COMPANY
  • 7. TANKS USED • Inlet channel • Bar screen • Course screen • Equalization tank • Pre-settler • Aeration tank • Secondary clarifier • Reaction tank • Tertiary clarifier • Tube settler • Thickener • Sludge sump
  • 8. MECHANICAL INSTRUMENTS USED • Pumps • Blowers • Rota meter • Agitators • Decenter • Rack arm
  • 9. BIO-AUGUMANTATION • It is a process of making new culture (Bacteria). Nutrition broth + media = fresh culture Fresh Culture + Water + jaggery New Culture (for aeration tank) air
  • 10. CHEMICAL PREPARATION For the dosing of chemicals in reaction tank and decenter we need to prepare the chemicals according to the demand of the effluent. 1. Poly electrolyte(anionic). 2. Poly electrolyte(cationic). 3. Poly aluminium chloride(PAC). Poly electrolyte(anionic). 10000 L of water + 1kg of poly electrolyte powder = poly electrolyte(anionic) solution.
  • 11. • Poly electrolyte(cationic). 10000 L of water + 1kg of poly electrolyte powder = poly electrolyte(cationic) solution Poly aluminum chloride. 9500 L of water + 500 L of concentrated PAC = poly aluminium chloride solution.
  • 12. CH-16 CH-1 TERTIARY CLARIFIER-1 TERTIARY CLARIFIER-1 PAC PE INFFLUENT INLET BAR SCREEN COURSE SCREEN GREASE & OIL CHAMBER EQUALIZATION TANK AIR PRE SETTLER UREA, DAP & BIOMASS SECONDRY CLARIFIER REACTION TANK AEREATIONTANK FINAL OUTLET INLET FROM CH-16 AIR 60% RECIRCULATION OF FRESH CULTURE DAP:- Di-ammonium Phosphate PAC:-Poly Aluminum Chloride PE:- Poly electrolyte(anionic) SC-1:- secondary clarifier CSS- Chemical Sludge Sump THK- Thickener To SC-1 CATEGORY-1 THK CSS CSS
  • 13. PAC PE INFFLUENT INLET BAR SCREEN COURSE SCREEN OIL & GREASE CHAMBER EQUALIZATION TANK SECONDRY CLARIFIER CAT-2 AEREATION TANK CAT-2 PRIMARY TUBE SETTLER CH-16 REACTION TANK-1 UREA, DAP & FRESH CULTURE PAC PE REACTION TANK-2 PE PAC TERTIARY TUBE SETTLER AEREATION TANK CAT-1 CH-1 UREA, DAP & MOLASSES ` AIR SECONDRY CLARIFIER CAT-1 REACTION TANK TERTIARY CLARIFIER-1 TERTIARY CLARIFIER-2 FINALOUTLET 60% RECIRCULATION OF BIOMASS CATEGORY-2 CSS CSS CSS TO THK TO THK
  • 14. CSS TERTIARY CLARIFIER-1 TERTIARY CLARIFIER-1 PAC PE INFFLUENT INLET BAR SCREEN COURSE SCREEN GREASE & OIL CHAMBER EQUALIZATION TANK AIR PRE SETTLER UREA, DAP & FRESH CULTURE SECONDRY CLARIFIER REACTION TANK AEREATIONTANK FINAL OUTLET CH-1 CH-8 INLET FROM CH-8 AIR 60% RECIRCULATION OF BIOMASS DAP- Di-ammonium Phosphate PAC-Poly Aluminum Chloride PE- Poly electrolyte(anionic) CSS- Chemical Sludge Sump CATEGORY-3 CSS SETTLED SLUDGE TO THICKNER
  • 15. EFFLUENT INLET BAR SCREEN COURSE SCREEN GREASE & OIL CHAMBER EQUALIZATION TANK AIR REACTION TANK-I TUBE SETTELER REACTION TANK-II FINAL OUTLET BLEACHING POWDER LIME CSS CATEGORY-4 HClPE
  • 16. 1. F/M = BOD×INFLUENT FLOW RATE MLVSS×AERATION TANK VOLUME Where, F = Food M = Microorganism MLVSS = Mixed Liquor Volatile Suspended Solids BOD = Biological Oxygen Demand 2. Treatment Charges = [0.02*So+0.03*(C-2.5*So) + 0.005*CSS+0.01*(C1- 2100)] x 1.10*[1 + R/100] y, Rs /KL Where, So = BOD of sample, mgs/L C = COD of sample, mgs/L Css = Suspended solids of sample, mgs/L C1 = TDS of sample, mgs/L R = Appreciation in each year. y = no. of years from base year 2011 FORMULAE
  • 17. SLUDGE Sludge is a semi-solid slurry and can be produced as sludge from wastewater treatment processes or as a settled suspension obtained from conventional drinking water treatment and numerous other industrial processes. There are two types of sludge. 1. Chemical sludge. 2. Bio-chemical sludge.
  • 18. SLUDGE DEWATERING Sludge dewatering is the separation of liquid and solid phase. For The Dewatering Of Sludge We Use Centrifuge/decenter.
  • 19. LAB TEST 1. Determination of chemical oxygen demand. 2. Determination of bio-chemical oxygen demand. 3. Determination of total suspended solid. 4. Determination of total dissolved solid. 5. Determination of pH. 6. Determination of dissolved oxygen.
  • 20. CONCLUSION Since the setting up of the CETP is a step towards reducing environmental pollution. and we know that Baddi is known as the hub of pharmaceutical industries in Asia. More industries at a particular place produces more effluent because of that nearby areas get more polluted. In such areas effluent treatment plant plays a vital role in protecting environment. According to my opinion in every industrial estate there must be a compulsory effluent treatment plant.