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“Lake Protection (Bandhwa Talab) through Decentralised 
Wastewater Management” 
“Lakes Bio-Remediation Project” 
WIPRO Corporate Office, Sarjapura, Bangalore 
25th November 2014 
Presented by Andrews Jacob
 Introduction to the Project 
 Current Sanitation Situation 
 Wastewater Management 
Concept (DEWATS) 
2 
PRESENTATION OUTLINE
INTRODUCTION TO PROJECT AREA 
3 
BANDHWA TALAB 
 Surface Area- 23,602 sq.mt. 
 Maximum depth- 230 cm 
 Status- 
• North Eastern edge- Untreated wastewater flow 
from adjacent Residential area, and surface 
drains convey solid waste 
• South East-an outflow drain present. Mainly 
used for laundry washing, fishing and religious 
activities 
• Western bank- Temple complex 
• South Eastern and South Western bank used 
for laundry washing 
• Fishing activities all around the lake. 
View on the eastern bank of Bandhwa Talab with 
lake water overrun at the north-eastern edge and 
rampant water vegetation. 
Bathing activities at the south-eastern bank. This 
part is free of water vegetation.
DEMOGRAPHY & LANDUSE 
4 
The catchment covers: 
 POPULATION- 916 persons 
 HOUSES-124 
 HOUSEHOLDS-171 
 AVERAGE HH SIZE-5 
 LANDUSE: 
 Residential-89% 
 Mixed-5% 
 Commercial- 5% 
 Institutional-2%
5 
WASTEWATER MANAGEMENT - MAP
6 
CURRENT SANITATION SITUATION… 
WASTEWATER MANAGEMENT 
COVERAGE OF SEPTIC TANKS EFFLUENT DISPOSAL FROM SEPTIC TANK
CONVEYANCE SYSTEM 
 Wastewater from households discharged into 
drains constructed for carrying storm water. 
 Total drain length in the catchment area 
approximately 1000 meters with depth varying 
from 0.3 to 0.8 meter 
 Type of existing drains are as follows: 
 Open Drains- 45% 
 Partially covered-26% 
 Fully Covered-22% 
 The overall condition of storm water drains is 
poor with more than 50% of total drain length 
clogged with solid waste. 
7 
CURRENT SANITATION SITUATION…
8 
CURRENT SANITATION SITUATION… 
DETAILS OF WATER BALANCE IN BANDHWA TALAB
9 
QUALITY OF WASTEWATER 
INFLOW AT BANDHUA TALAB: 
 Chemical Oxygen Demand 
(COD) -310 to 1183 mg/l. 
 Biological Oxygen Demand 
(BOD) -103 to 392 mg/l. 
AT BYPASS: 
 COD -734 to 1550 mg/l and 
 BOD -234 to 512 mg/l 
BANDHWA 
TALAB 
BYEPASS 
CURRENT SANITATION SITUATION… 
Wastewater quality analysis conducted 
during period May-July 2012
CONCEPT FOR WASTEWATER MANAGEMENT 
10 
Finalised Concept 
The above mentioned concept was approved by RMC Officials on 20/12/2012 
and the decentralised technology for wastewater treatment selected was 
DEWATSTM for its low O&M cost in comparison to the other technologies.
11 
POTENTIAL OF DIFFERENT TREATMENT OPTIONS 
Criteria SBR DEWATS FAB 
Performance in Terms of Quality of Treated Sewage 
Potential of Meeting the TSS, BOD, and COD 
Discharge Standards 
Potential of Total / Faecal Coliform Removal 
Potential of DO in Effluent 
Potential for Nitrogen Removal (Nitrification- 
Denitrification) 
Potential for Phosphorous Removal 
Performance Reliability 
Potential of Low Energy Requirement 
Potential of Low Land Requirement 
Potential of Low Capital Cost 
Potential of Low Recurring Cost 
Potential of Low Level of Skill in Operation 
Potential of Low Level of Skill in Maintenance 
Potential Low Medium High Very High
12 
INPUT DATA FOR DPR 
 Catchment population - 1000 people 
 Water Supply - 135 lpcd (based on the service level 
benchmarks as mentioned in the CSP for Raipur City). 
 Wastewater generation - 85% of water supply i.e. 114.75 cu.m 
per day (say 115 cu.m/day) 
 Composition of wastewater 
 67% greywater, 33% blackwater. 
 Greywater generated - 76.38 cu.m/day (say 77 cu.m) 
 Blackwater generated - 37.86 cu.m/day (say 38 cu.m/day)
13 
INPUT DATA FOR DETAILING CONCEPT 
Wastewater parameters for designing of treatment unit 
Parameter Grey Water 
Blackwater 
(effluent from 
septic tank) 
Combined 
(grey+black) 
Biological Oxygen Demand (BOD) 
mg/L 
100 - 150 300 - 450 200 - 400 
Chemical Oxygen Demand (COD) 
mg/L 
200 - 300 600 - 900 400 - 800 
Total Solids mg/L 500 - 700 800 - 1000 100 - 150 
Total Nitrogen mg/L 0.05 - 0.15 0.05 – 0.15 0.15 – 0.20 
Phosphates (as P) mg/L 3.00 – 5.00 5.00 – 10.00 10 - 15 
Coliform (MPN/100 ml) 1600 > 1600 1000 - 1600 
Based on wastewater quality analysis conducted during period May-July 2012
15 
DETAILS OF DPR 
locations for installation of 
treatment unit 
 Two potential sites available for 
installation of treatment unit. 
 Preferred location - land identified in 
the northern part of Bandhwa Talab 
(Site A) close to the inlet point 
 The other location is a low lying area 
in the north eastern part of the lake 
(Site B). 
SITE ‘A’ 
SITE ‘B’
16 
Stakeholder Workshop 
“GIZ Support to the NUSP – CSP Implementation” 9th April 2013, Raipur
17 
Stakeholder Workshop 
“GIZ Support to the NUSP – CSP Implementation” 9th April 2013, Raipur
18 
Proposed Network for Conveying Wastewater 
Stakeholder Workshop 
“GIZ Support to the NUSP – CSP Implementation” 20 December 2012, Raipur
19 
DETAILS OF FINALISED CONCEPT… 
Treatment and Disposal 
 The quantum of wastewater to be treated is estimated to be 115 cu.m. 
 The wastewater shall be treated using a DEWATSTM technology to a 
level prescribed by PCB and shall be discharged into Bandhwa Talab
20 
DETAILS OF TREATMENT TECHNOLOGY 
Decentralised Wastewater 
Treatment System (DEWATSTM) 
The wastewater collected through the 
SSS shall be conveyed through the 
following modules for treatment: 
 Settler – Primary treatment 
 Anaerobic Baffled Reactor (ABR) – 
secondary treatment and organic reduction 
upto 90% can be achieved 
 Anaerobic Filter (AF) - further 70-90% of the 
remaining organic load 
 Planted Gravel Filter (PGF) –tertiary 
treatment for further removal of organic load 
and nutrients present in the wastewater 
Collectio 
n Tank 
Pump wastewater to Lake
TREATMENT MODULE 1 - SETTLER 
Scum 
 Sedimentation tank for retaining settleable particles 
 Dissolved and suspended matter passes untreated to 
next stage of treatment 
 Efficiency of 25% - 40% 
 Desludging period of 2 years as per design for 
sludge storage 
21 
Raw 
Sewage 
Partially Treated 
Wastewater 
Sludge Sludge 
Biogas 
Gas
22 
TREATMENT MODULE 2 – ANAEROBIC BAFFEL REACTOR + 
ANAEROBIC FILTER 
Gas Gas Partially Treated 
Wastewater 
Activated 
Sludge
23 
TREATMENT MODULE 2 – ANAEROBIC BAFFEL REACTOR + 
ANAEROBIC FILTER… 
Anaerobic Baffle Reactor (ABR): 
• Anaerobic treatment (in the absence of oxygen) 
• Wastewater passes a series of up-flow chambers 
• Bacteria mass (activated sludge) at bottom of each chamber 
• Further treatment (degradation) of suspended and dissolved solids by 
anaerobic bacteria 
• Efficiency 75% - 85% 
Anaerobic Filter (integrated with ABR) 
• Wastewater passes in a series of up-flow chambers with carrier 
material (filter material) 
• The filter is made out of gravel, slag or plastic elements 
• To avoid plugging pre-treatment (sedimentation) is necessary. 
• Efficiency 75% - 90%
24 
TREATMENT MODULE 3 – PLANTED GRAVEL FILTER 
 Aerobic treatment (in the presence of 
oxygen) 
 Planted Gravel Filter (PGF) consist of plants 
(reeds) & filter materials (graded gravels, 
river pebbles) 
 The filter is permanently soaked (up to 50 
cm from bottom) in water 
 The flow direction is horizontal 
 Wastewater requires pre-treatment
29 
O&M 
Desludging of settler Wastewater Monitoring 
Cleaning of filter material Plant harvesting for PGF
 Treatment is based on physical and 
biological (anaerobic and aerobic) 
wastewater treatment component 
 Affordable price 
 Fulfillment of discharge standards 
 Treatment of wastewater flows from 1-1000 
m3/d 
 Tolerance to inflow fluctuation 
 No dependence on external energy 
 Minimal and easy maintenance 
 Reliability and long-lasting 
 Reuse of wastewater 
30 
ADVANTAGES OF DEWATS TECHNOLOGY
Consortium for DEWATS Dissemination (CDD) Society 
Survey No. 205, (Opp. Beedi Workers Colony) 
Kommaghatta Road, Bandemath 
Kengeri Satellite Town 
Bangalore 560 060 – Karnataka, India 
Tel/Fax: +91-080-28486700 / 28482144 
THANK YOU… 
www.cddindia.org 
Follow us:

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How DEWATS can be implemented to bio-remediate lakes

  • 1. “Lake Protection (Bandhwa Talab) through Decentralised Wastewater Management” “Lakes Bio-Remediation Project” WIPRO Corporate Office, Sarjapura, Bangalore 25th November 2014 Presented by Andrews Jacob
  • 2.  Introduction to the Project  Current Sanitation Situation  Wastewater Management Concept (DEWATS) 2 PRESENTATION OUTLINE
  • 3. INTRODUCTION TO PROJECT AREA 3 BANDHWA TALAB  Surface Area- 23,602 sq.mt.  Maximum depth- 230 cm  Status- • North Eastern edge- Untreated wastewater flow from adjacent Residential area, and surface drains convey solid waste • South East-an outflow drain present. Mainly used for laundry washing, fishing and religious activities • Western bank- Temple complex • South Eastern and South Western bank used for laundry washing • Fishing activities all around the lake. View on the eastern bank of Bandhwa Talab with lake water overrun at the north-eastern edge and rampant water vegetation. Bathing activities at the south-eastern bank. This part is free of water vegetation.
  • 4. DEMOGRAPHY & LANDUSE 4 The catchment covers:  POPULATION- 916 persons  HOUSES-124  HOUSEHOLDS-171  AVERAGE HH SIZE-5  LANDUSE:  Residential-89%  Mixed-5%  Commercial- 5%  Institutional-2%
  • 6. 6 CURRENT SANITATION SITUATION… WASTEWATER MANAGEMENT COVERAGE OF SEPTIC TANKS EFFLUENT DISPOSAL FROM SEPTIC TANK
  • 7. CONVEYANCE SYSTEM  Wastewater from households discharged into drains constructed for carrying storm water.  Total drain length in the catchment area approximately 1000 meters with depth varying from 0.3 to 0.8 meter  Type of existing drains are as follows:  Open Drains- 45%  Partially covered-26%  Fully Covered-22%  The overall condition of storm water drains is poor with more than 50% of total drain length clogged with solid waste. 7 CURRENT SANITATION SITUATION…
  • 8. 8 CURRENT SANITATION SITUATION… DETAILS OF WATER BALANCE IN BANDHWA TALAB
  • 9. 9 QUALITY OF WASTEWATER INFLOW AT BANDHUA TALAB:  Chemical Oxygen Demand (COD) -310 to 1183 mg/l.  Biological Oxygen Demand (BOD) -103 to 392 mg/l. AT BYPASS:  COD -734 to 1550 mg/l and  BOD -234 to 512 mg/l BANDHWA TALAB BYEPASS CURRENT SANITATION SITUATION… Wastewater quality analysis conducted during period May-July 2012
  • 10. CONCEPT FOR WASTEWATER MANAGEMENT 10 Finalised Concept The above mentioned concept was approved by RMC Officials on 20/12/2012 and the decentralised technology for wastewater treatment selected was DEWATSTM for its low O&M cost in comparison to the other technologies.
  • 11. 11 POTENTIAL OF DIFFERENT TREATMENT OPTIONS Criteria SBR DEWATS FAB Performance in Terms of Quality of Treated Sewage Potential of Meeting the TSS, BOD, and COD Discharge Standards Potential of Total / Faecal Coliform Removal Potential of DO in Effluent Potential for Nitrogen Removal (Nitrification- Denitrification) Potential for Phosphorous Removal Performance Reliability Potential of Low Energy Requirement Potential of Low Land Requirement Potential of Low Capital Cost Potential of Low Recurring Cost Potential of Low Level of Skill in Operation Potential of Low Level of Skill in Maintenance Potential Low Medium High Very High
  • 12. 12 INPUT DATA FOR DPR  Catchment population - 1000 people  Water Supply - 135 lpcd (based on the service level benchmarks as mentioned in the CSP for Raipur City).  Wastewater generation - 85% of water supply i.e. 114.75 cu.m per day (say 115 cu.m/day)  Composition of wastewater  67% greywater, 33% blackwater.  Greywater generated - 76.38 cu.m/day (say 77 cu.m)  Blackwater generated - 37.86 cu.m/day (say 38 cu.m/day)
  • 13. 13 INPUT DATA FOR DETAILING CONCEPT Wastewater parameters for designing of treatment unit Parameter Grey Water Blackwater (effluent from septic tank) Combined (grey+black) Biological Oxygen Demand (BOD) mg/L 100 - 150 300 - 450 200 - 400 Chemical Oxygen Demand (COD) mg/L 200 - 300 600 - 900 400 - 800 Total Solids mg/L 500 - 700 800 - 1000 100 - 150 Total Nitrogen mg/L 0.05 - 0.15 0.05 – 0.15 0.15 – 0.20 Phosphates (as P) mg/L 3.00 – 5.00 5.00 – 10.00 10 - 15 Coliform (MPN/100 ml) 1600 > 1600 1000 - 1600 Based on wastewater quality analysis conducted during period May-July 2012
  • 14. 15 DETAILS OF DPR locations for installation of treatment unit  Two potential sites available for installation of treatment unit.  Preferred location - land identified in the northern part of Bandhwa Talab (Site A) close to the inlet point  The other location is a low lying area in the north eastern part of the lake (Site B). SITE ‘A’ SITE ‘B’
  • 15. 16 Stakeholder Workshop “GIZ Support to the NUSP – CSP Implementation” 9th April 2013, Raipur
  • 16. 17 Stakeholder Workshop “GIZ Support to the NUSP – CSP Implementation” 9th April 2013, Raipur
  • 17. 18 Proposed Network for Conveying Wastewater Stakeholder Workshop “GIZ Support to the NUSP – CSP Implementation” 20 December 2012, Raipur
  • 18. 19 DETAILS OF FINALISED CONCEPT… Treatment and Disposal  The quantum of wastewater to be treated is estimated to be 115 cu.m.  The wastewater shall be treated using a DEWATSTM technology to a level prescribed by PCB and shall be discharged into Bandhwa Talab
  • 19. 20 DETAILS OF TREATMENT TECHNOLOGY Decentralised Wastewater Treatment System (DEWATSTM) The wastewater collected through the SSS shall be conveyed through the following modules for treatment:  Settler – Primary treatment  Anaerobic Baffled Reactor (ABR) – secondary treatment and organic reduction upto 90% can be achieved  Anaerobic Filter (AF) - further 70-90% of the remaining organic load  Planted Gravel Filter (PGF) –tertiary treatment for further removal of organic load and nutrients present in the wastewater Collectio n Tank Pump wastewater to Lake
  • 20. TREATMENT MODULE 1 - SETTLER Scum  Sedimentation tank for retaining settleable particles  Dissolved and suspended matter passes untreated to next stage of treatment  Efficiency of 25% - 40%  Desludging period of 2 years as per design for sludge storage 21 Raw Sewage Partially Treated Wastewater Sludge Sludge Biogas Gas
  • 21. 22 TREATMENT MODULE 2 – ANAEROBIC BAFFEL REACTOR + ANAEROBIC FILTER Gas Gas Partially Treated Wastewater Activated Sludge
  • 22. 23 TREATMENT MODULE 2 – ANAEROBIC BAFFEL REACTOR + ANAEROBIC FILTER… Anaerobic Baffle Reactor (ABR): • Anaerobic treatment (in the absence of oxygen) • Wastewater passes a series of up-flow chambers • Bacteria mass (activated sludge) at bottom of each chamber • Further treatment (degradation) of suspended and dissolved solids by anaerobic bacteria • Efficiency 75% - 85% Anaerobic Filter (integrated with ABR) • Wastewater passes in a series of up-flow chambers with carrier material (filter material) • The filter is made out of gravel, slag or plastic elements • To avoid plugging pre-treatment (sedimentation) is necessary. • Efficiency 75% - 90%
  • 23. 24 TREATMENT MODULE 3 – PLANTED GRAVEL FILTER  Aerobic treatment (in the presence of oxygen)  Planted Gravel Filter (PGF) consist of plants (reeds) & filter materials (graded gravels, river pebbles)  The filter is permanently soaked (up to 50 cm from bottom) in water  The flow direction is horizontal  Wastewater requires pre-treatment
  • 24. 29 O&M Desludging of settler Wastewater Monitoring Cleaning of filter material Plant harvesting for PGF
  • 25.  Treatment is based on physical and biological (anaerobic and aerobic) wastewater treatment component  Affordable price  Fulfillment of discharge standards  Treatment of wastewater flows from 1-1000 m3/d  Tolerance to inflow fluctuation  No dependence on external energy  Minimal and easy maintenance  Reliability and long-lasting  Reuse of wastewater 30 ADVANTAGES OF DEWATS TECHNOLOGY
  • 26. Consortium for DEWATS Dissemination (CDD) Society Survey No. 205, (Opp. Beedi Workers Colony) Kommaghatta Road, Bandemath Kengeri Satellite Town Bangalore 560 060 – Karnataka, India Tel/Fax: +91-080-28486700 / 28482144 THANK YOU… www.cddindia.org Follow us:

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