KARNATAKA URBAN WATER SUPPLY & DRAINAGE BOARD BANGALORE PRESENTATION ON WATER SUPPLY MANAGEMENT By K.P. Jayaramu, Executive Engineer, Karnataka Water Board, Jn NURM City Division, Mysore Responsibility of KUWS & DB in Hubli-Dharwad Before 3/2003: O & M of bulk WSS After 3/2003: : KUWS & D Board O & M of Distribution System : HDMC As per G.O. No.UDD25.2002 B’lore Dtd:24-03-03 O & M of both bulk & Distribution – KUWS & DB. Main Contents of G.O. No.UDD25.2002 B’lore Dtd:24-03-03 Status • Poor Water Service levels due to improper maintenance • Huge gap between Income & Expenditure. Targets • To improve the Service level thro’ control of UFW, illegal connections, etc. • To reduce huge gap between Income and Expenditure HUBLI N R BETTA GLSR GRAVITY MAIN 600MM 3.0 KM KESHWAPUR RISING MAIN 1168 MM 23 KM GLSR GRAVITY MAIN 800MM 8.75 KM MALAPRABHA RESERVOIR GRAVITY MAI 600MM 15.7K H.S.R Saraswtpur GRAVITY MAIN RISING MAIN RISING MAIN 600MM 8.25KM 965 MM 30 KM TREATMENT PLANT & PUMPHOUSE 750MM 12.2 KM K. HONNAPUR Treatment Plant AMMINBHAVI DHARWAD RISING MAIN 450MM 9.3 KM DUMWAD PUMPHOUSE RISING MAIN 762MM 6.7 KM GRA 750 M NEERSAGAR WATER SUPPLY MANAGEMENT WATER SUPPLY MANAGEMENT • Bulk Water Supply System - Simple • Water Distribution System - Complex Types of Water Distribution System • 24x7 Water Supply System • Intermittent Water Supply System Sources & Bulk Supply Sl. No. 1 2 Water Level(Mtr) Dead Storage Full Present Level 633.84 623.08 619.51 Live Storage TMC Reservoir Malaprabha Neerasagar (2079') (2043.73') ( 2032') 590.85 589.00 587.79 (1932.3") (1906.0 ”') (1938') Total System Capacity MLD TMC Total Present Total Dwd Hubli Total 3.38 35.05 7.09 140 70 66 136 0.09 0.924 0.7 52 0 31 31 3.47 35.97 30.15 192 70 97 167 Status of Borewells Malaprabha Reservoir Neerasagar Reservoir Actual Supply MLD Power Pump Hand Pump Hubli 812 444 Dharwad 321 239 Total 1133 683 Approximate Qty from Borewell source : 5MLD – Hubli 2.5MLD -Dharwad TECHNICAL CHALLENGES •Absence of Master planning •Lack of Zoning •Insufficient Reservoirs & feeder mains in New Extensions • Power Problems: More No of Power failures - Average : 55 times/ month Frequency variation - 50 Hz Fr. varies to 48.5 Hz •Huge Water losses in Sub-standard quality of PVC pipes in about 60% areas Average Pipe Leakages : Before 9/2011 After 9/2011 Hubli - 300/ month - 412/ month Dharwad– 125/ month – 225/ month LEAKAGES IN PVC PIPES • Insufficient Skilled Staff • G.O.(No. LD 275 LWA 05 Dt.2-77-05), banning Contract labour hinders Outsourcing Smart Water Supply Message Service HDMC Resolution No 828 Dated 30-08-2011 “Smart Water Supply Message Service” by MS graduates from Berkley University, US. ` 10 per Month for General Customers & ` 5 per Month for Urban poor The Service is Optional Live Dashboard DATE VALVEMEN ID vm106 vm103 vm103 vm101 vm101 vm103 vm103 vm103 1/1/2012 vm103 vm103 vm103 vm103 vm103 vm103 vm106 vm106 vm106 vm103 WARD NO Ward 26 Ward 27 Ward 27 Ward 25 Ward 25 Ward 27 Ward 27 Ward 27 Ward 27 Ward 27 Ward 27 Ward 27 Ward 27 Ward 27 Ward 26 Ward 26 Ward 26 Ward 27 NOTICE opened opened closed opened closed opened opened closed opened closed opened closed opened closed opened opened closed opened AREA Acchhvvana colony Attigere Layout Attigere Layout Eshwar nagar Eshwar nagar Kalidas Nagar Kalyan Nagar Kalyan Nagar Lingarajnagar North Lingarajnagar North Lingrajnagar South Lingrajnagar South Patil Layout Patil Layout Sai nagar Siddeshwara Nagar Siddeshwara Nagar Siddeshwara park TIME 19:08 7:02 12:44 7:44 19:17 10:33 7:01 9:29 7:00 9:27 7:11 13:31 7:02 9:31 19:08 16:08 20:25 12:43 DURATION (Hours) SUPPLY CYCLE 5.7 2 11.55 2 2 2.47 2 2.45 2 6.33 2.48 2 2 2 4.28 2 Smart Water Supply Message Service "Control Station" for monitoring Water Supply in Hubli Duty Chart Date From To From To From To 7:00 AM 2:00 PM 1:00 PM 9:00 PM 8:00 PM 8:00 AM 01-08-2011 E 2 & M.S.Hosmani E 3 & A.S.Ganjihal E 1 & R.K.Umesh 02-08-2011 E 3 & B.H.Giriyammanavar E 4 & B.R.Haveli E 2 & D'souza 03-08-2011 E 1 & S.K.Hegde E 4 & Dejappa E 3 & M.Mishrikoti E 4 & Guruprasad.Pawar E 1 & S.M.Hubli 04-08-2011 E 2 & V.V.Giddalingannavar 05-08-2011 E 3 & Santosh.R E 4 & R.V.Patil E 2 & R.N Hazeri 06-08-2011 E 1 & H.Ravindra E 4 & M.Madaiah E 3 & M.M.Chavhan 07-08-2011 (Sunday) E 2 & S.Y.Merawde E 1 & Basavaraj.Madivalar E 4 & B.S.Srinivas On-Line Bulk Flow Monitoring System On-Line Vehicle Tracking System for Tankers On-Line Vehicle Tracking System for Tankers NRW in Hubli-Dharwad Standard Water Balance Recommended by International Water Association (IWA ) Billed Metered Consumption Billed Authorized Consumption Authorized Consumption System Input Volume Water Losses (UFW) Billed Unmetered Consumption Unbilled Authorized Consumption Unbilled Metered Consumption Apparent Losses Unauthorized Consumption Unbilled Unmetered Consumption Metering Inaccuracies and Data Handling Errors Physical Losses Revenue Water Leakage on Transmission and/or Distribution Mains Leakage and Overflows at Storage Tanks Leakage on Service Connections up to Customer Meter NonRevenue Water IWA - Standard Water Balance - Calculations Sl No Particulars Quantity per month in ML Demozone ( ML) Total ML Non-Demozone ( ML) 1 Billed Metered consumption 2 145.00 355.50 500.50 2.1 Low pressure areas 17769 x 15000 / 106 = 266.50 266.50 2.2 Unmetered consumption 15617 x 20000 / 106 = 312.34 312.34 15 x 3500 +15 x 7000 / 106 = 0.16 0.16 Billed unmetered Consumption 2.3 Tanker Supply (paid) 3 Unbilled metered consumption 4 More than 50 KL 15.00 Unbilled unmetered consumption Tankers 1200 x 7000 / 106 = 8.40 Tractors 500 x 4000 / 106 = 2.00 10.40 135.00 135.00 BW 494 x 25000 / 106 =12.35 12.35 Unauthorized consumption 3000 x 20000 / 106 = 60.00 60.00 Customer Meter inaccuracies 10000 x 5000 / 106 = 50.00 50.00 325.23 343.23 70.00 70.00 2.00 232.52 234.52 180.00 1830.00 2010.00 4.1 Tanker supply (free) (to Govt. Schools, slums, etc) 4.2 Bore well water supply 4.3 Public stand posts 5 15.00 6 7 Leakage of Transmission & Distribution mains 8 Leakage & overflow at Storage Reservoirs 9 Leakage on service connection upto customer meter. Total 18.00 Standard Water Balance Recommended by International Water Association (IWA ) Billed Authorized Consumption Authorized Consumption 1243.25 ML 62 % System Input Volume 2010 ML Water Losses (UFW) 766.75ML 1079.50 ML 54 % Billed Metered Consumption 500.5 24.9 % Billed Unmetered Consumption 579.0 ML 28.8 % Unbilled Authorized Consumption 163.75 ML 8% Unbilled Metered Consumption 15.00 ML 0.7 % Apparent Losses Unauthorized Consumption 60.00 ML 2.9 % 110.00 ML 5% Metering Inaccuracies and Data Handling Errors 50.00 ML 2.5 % Physical Losses Leakage on Transmission and/or Distribution Mains 343.23 ML 17.0 % 656.75ML Unbilled Unmetered Consumption 157.75 ML 7.8 % Revenue Water 1079.5 54% NonRevenue Water 930.50 ML 46% Action plan for NRW reduction Reduction of Physical losses Water losses minimising policies MD KUWS & DB ORDER DATED 25-7-2007 to replace PVC Pipes by HDPE & DI/MS Pipes More Water losses in PVC pipes In Corporation Areas : HDPE Pipes upto 250 mm dia DI/MS pipes above 250 mm dia Action plan for NRW reduction Reduction of Physical losses Water losses minimising policies HDMC Resolution No.221, DATED 14-12-2007 • House Service Connections at departmental cost • Maintenance of HSCs at departmental cost Typical Service Connection on PVC pipes Typical House Service Connection On HDPE Pipe Action plan for NRW reduction Reduction of Physical losses • Attending leakages in reservoirs • Avoiding overflows Grouting for NR Betta GLSR Grouting for Rayapur GLSR Improvements in Water Supply in Hubli-Dharwad Particulars Hubli Dharwad Supply Periodicity Before 2003 Once in 7 days Once in 7 days Supply Periodicity After 2003 upto 9/2011 Once in 5 days Once in 4 to 5 days Supply Periodicity After 9/2011 Once in 2 days- 75% Once in 3 days- 25% Once in 2 days- 70% Once in 3 days- 30% Supply Duration 2 to 3 hours duration 2 to 3 hours duration 7 6 88 52 978 857 Master Zones No. of Valve men No. of Valves operated /supply Comparison between 24x7 and Intermittent Water Supply System Particulars Intermittent Water Supply System, Hubli 24X7 Water Supply Demo zone, Hubli Once in 2 to 3 days for 2 to 4 hours duration Continuous 6 1 Sub Zones 700 119 No. of Valve men 88 Nil No. of Valves operations /cycle 978 Nil No. of Pressure Reducing Valves Nil 13 60738 8148 Number of Technical Staff 21 3 Staff per 1000 Connections 6 1 Supply Pattern Zones No. of Connections Features of 24x7 Water Distribution System in Hubli • Average per capita consumption is 129 LPCD (17 % less) • Actual average NRW – 14 % • Average actual physical losses 5 liters/ connection/ day/ meter pressure (Allowable 30 to 20 liters) • No public fountains, all Urban Poor connected • Urban poor (~25%) consume at 55 LPCD • Pay ` 48/month for 8 KL / month Financial Reforms Customer friendly Reforms IT Enablement in Customer services Transparency in O & M Activities Financial Reforms in Hubli-Dharwad WSS Tariff Revision Metering Pro-rata charges Customer Services Computerized Billing, Accounting & Revenue Collection Increase in Cost Recovery Better Water supply Tackling unauthorized connections Computerized Billing, Accounting Method Sl.No Activity Before 3/2003 After 3/2003 1 Billing Method Manual Spot billing through Hand held computers 2 Billing Periodicity Irregular Monthly Reading cards with Customer’s signature, 3 Customer interaction Not much Customer Care Centre. 4 Accounting Accuracy Not accurate Very accurate, Monthly auditing by CA 5 Various Reports Not possible Possible Hand held Computer for Spot billing The bill is printed on to the blue tooth printer carried by the meter reader and is updated to the server online along with the image and GPS coordinates . Computerized Revenue Collection Method Sl.No Activity Before 3/2003 After 3/2003 1 Collection Method 3 Bank Counters 14 Cash Counters and 7 H-D 1 Centers 2 Waiting Period More than 15 minutes 3 to 15 minutes 3 Part payment After approval Allowed without any approval 4 Identity Card No Tap Cards with bar-coding being issued For bill payment without producing bill also 5 No. of paid bills (monthly) About 15000 About 60000 H-D 1 Center, Hubli Customer Services through SAKALA and Hubli-Dharwad One centers HUBLI DHARWAD one ONE STOP NON STOP SERVICES Free Issue of New connection applications in HD-1 and New connection under SAKALA Payments of New connection Fees based on Unique ID. Payments of Monthly bills. Issue & Acceptance of Application for : Change of Name / Size/ Purpose Rs 100 : Meter Installation, Rs 128 : Meter repair/shifting/ Re-location, Fee Rs 100 : Tap repair/Re-location, Fee Rs 100 : Tap Re-connection & Disconnection . e-Tracking System for above Services : All these Services to citizens With Home Environment through HD1 Fixed Time Limit No middle men Timings from 8 AM TO 8 PM on all 365 days Hubli Dharwad One Center One stop non stop service Working Hours 8:00 am to 8:00 pm, on all 365 days METERING Metering Process • Division of Supply Areas into Non-Low & Low Pressure Zones. • Water Meters fixed in Non-Low pressure Zones. • Low Pressure Zones have been tackled after making improvements. • Campaign-media, press, cable TV, Posters, hand bills, mike, customer meetings. • Freedom to customers to purchase tested meters from market. • Departmental help to fix the meters. Metering Status in Hubli - Dharwad Year Before 3/2003 (HDMC) No of connections No of Connections with working meters % of Metered Connection 68,997 Nil Nil As on 3/2013 (KUWS & DB) Hubli-Dharwad Non-Demo zone 24x7 Demo zone Hubli-Dharwad 1,04,887 70,565 14,721 14,721 1,19,608 85,286 67% 100% 71% Water Tariff Structure in Hubli-Dharwar Before 2003 Water Rate in ` per 1000 Liters Dom Effective Date Range 0 - 50000 50001-Above One lakh Min Charges/Month 1/10/1986 1/10/1996 Non-Dom Rate 0-25 to 0-70 0-90 to 4-00 Com/Ind Range Rate Range All 6-00 All 4-00 20-00 Rate 8-12 25-00 Taps without Meters ½" 8-00 25-00 ¾" 15-00 50-00 1" 30-00 100-00 2" 60-00 200-00 0 - 50000 1-26 to 2-66 3-32 to 4-32 50001 - Above 1 Lakh 1-66 to 6-16 5-32 to 7-32 45 90 Min Charges /Month All 8-64 180 Water Tariff revision in Hubli-Dharwar After 2003 Water Rate in ` per 1000 Liters Effective Date Dom Range Non-Dom Rate No change Com/Ind Range Rate Range Rate All Range 11-60 All Range 23-20 60/04/040/04 1/4/2005 Min Charges per month All Range 45-00 5-80 All Range 90-00 11-6 Order No.HDMC/ 180-00 All Range 23-20 1/8/2005 Dt:2-05-2005 Order No.HDMC/ 60/01/05 Min Charges per month 90-00 180-00 360-00 Dt:31-08-2005 PRORATA CHARGES FOR NEW CONNECTIONS HDMC Resolution No.824 & 936 Dated 28-05-04 • Retail Customers: ` 76/Sq.m of Plinth area • A concession of 50% for Declared slums • Not applicable for Poor SC/ST customers • Not applicable for Poor customers with Building plinth area less thsn 600 Sq.ft. • For Com/Industrial connections 50% more • For domestic customers, maximum ` 10000 • For half inch sized Commercial/Industrial connections, maximum ` 25000 • Bulk Customers : ` 12500 per KL Prorata charges collected (From 2004 to 3/2012) (in ` Lakhs) Hubli Dharwad Total 717 330 1047 PRORATA CHARGES Method of Calculation : For Bulk Consumers 1. Capital Cost Est cost of EIWSS (Revised) Scheme Est Cost of A ugmentation of Water Transmission System in Hubli Dharwad Twin Cities = Rs. 49.17 Crores = Rs. 42.42 Crores Total = Rs. 91.59 Crores Est Capital Cost = Rs. 92.00 Crores 2. Unit Prorata Cost Quantity of Water produced Prorata Cost = 92.00 x 100 73.80 = 73.80 MLD = 124.66 lakhs/MLD Say 125.00 lakhs/ MLD 3. Calculation of Prorata Cost for Railways, Hubli Ultimate Requirment of Water 5.45 MLD Prorata Cost = 125.00 X 5.45 = Rs.681.25 Lakhs A pproximate Cost of Dedicated Water Supply Scheme to Railways, Hubli Rs 2400.00 Lakhs Hence, it is economical to get water from Hubli-Dharwad water supply scheme by paying prorata cost. PRORATA CHARGES Method of Calculation : For Retail Consumers 1) Prorata Cost towards Bulk W/S Scheme 1.1) Capital Cost Est. Cost of EIWSS (Revised) Scheme to Hubli Dharwad . . . . . Rs. 63.84 Crores Est. Cost of Transmission Main from Amminbhavi to Hubli . . . . Rs. 36.00 Crores TOTAL . . . . . . Rs. 99.84 Crores Est. Capital Cost Say, . . . . . Rs. 100.00 Crores Deduct Govt. Grant of 23 1/3% (-) Rs. 23.33 Crores BALANCE Rs. 76.67 Crores 1.2) Unit Prorata Cost Quantity of Water produced = 73.80 + 40.0 MLD =113.80 MLD Unit Prorata Cost / KLD = 76.67 x 10000000 113.80 x 1000 = Rs. 6737.00 1.3) Calculation of Prorata Cost towards Bulk, W S S Assuming rate of supply as 135 LPCD & 5 persons per house Water Quantity per site= 135 x 5 = 675.00 Liters/day = 0.675 KLD Prorata Cost per house = 0.675 x 6737.00 = Rs. 4547.48 Say Rs. 4548.00 For each house taking Floor Area =150.00 Sqm Therefore, Prorata cost per Sqm of Floor area = 4845 / 150 = Rs. 30 Say Rs. 30.00 per Sqm of floor area. PRORATA CHARGES 2. Prorata towards Feeder Network and Reserviors. Cost of Feeder Network and Reservoirs . . . . . Rs. 100.00 Crores Deduct Govt, Grant 23 ½ % . . . (-) Rs. 23.33 Crores Balance Cost . . . . . Rs. 76.67 Crores Present population (Projected for 2003) = 8.50 Lakhs Assuming 5 persons per House Cost per House = 76,67,00,000 x 5 -------------------- = Rs. 4510 850.00 Taking Floor up area as 150 Sqm Prorata cost per Sqm of floor area = 4510.00 ---------150.00 = Rs. 30.06 Say Rs. 30.00 per Sqm of floor area. PRORATA CHARGES 3. Prorata Cost towards Pipe net work: Approximate cost of service pipe network in individual layouts is calculated for 1 The actual cost will depend on detailed surveys and estimation. Sl. No Pipe Dia and Material running meter. Cost of Pipe of laying charges (Rs.) 70.95 Cost of Excavation & Refilling (Rs) 43.16 Total Cost (Rs.) 114.11 1 90 mm dia x 6 KSC PVC 2 110 mm dia x 6 KSC PVC 101.80 43.16 144.96 3 150 mm dia Kg DI 724.00 58.86 782.86 Total 1041.93 Average Cost 347.31 Deduct 23.33 % Government Grant Taking 50 % of Rs. 270.00 for one side (-) 81.03 Balance 266.28 Say 270 I.e Rs. 135.00 per M width of site. PRORATA CHARGES Prorata Charges for different sites : 6x9M 6 x 135 = Rs. 810.00 40 M2 Rs. 20-25 9 x 12 M 9 x 135 = Rs. 1215.00 75 M2 Rs. 16.20 12 x 18 M 12 x 135 = Rs. 1620.00 150 M2 Average Rs 10.80 Rs. 15-75 Say Rs. 16.00 PRORATA CHARGES Abstract Sl. No Beneficiaries Rate per Prorata Charges Rs. For Sqm of 6 x 9 M 9 x 12 M 12 x 18 M Floor For floor area of area 40 M2 75 M2 150 M2 For Residential buildings in authorized 1 layouts, unauthorized layouts and Apartments Towards Malaprbaha W/S Scheme (This is 1.1 exempted if paid earlier) 30/- 1200/- 2400/- 4800/- 1.2 Towards feeder Network and Reservoir 30/- 1200/- 2400/- 4800/- 16/- 640/- 1280/- 2560/- Towards Service Pipe net work (This is 1.3 exempted if the layouts has proper net work as per standard quality and designs) REGULARISATION OF ILLEGAL CONNECTIONS Special camps for regularization of illegal connections • RR No’s painted on compounds to identify illegal connections. • Special camps for regularization of illegal connections chaired by the local Corporators. • NGO’s have been involved. • Campaign through media, press, cable TV, Posters, hand bills, mike, customer meetings. • Mobile bank arranged. Status of of Illegal Connections Year No of connections No of Illegal Connections Before 3 / 2003 ( HDMC) As on 8/2002 68,997 21,072 30.50 % After 3 / 2003 ( KUWS & DB) As on 3/2013 1,19,608 3,260 2.7 % Measures to avoid Illegal connections Typical House Service Connection on PVC pipes ( Old ) Departmental Implementation of HSCs HDMC Resolution No 221 Dated 14-12-2007 Features : House Service Connections at departmental cost Maintenance of HSCs at departmental cost Fees for Change of Connection exempted Typical House Service Connection On HDPE Pipes Benefits: • Control of Quality and Workmanship • Huge losses in HSC avoided • Illegal connections avoided Issue & processing new connections applications at HD-1 centers( 8 am to 8 pm) Easy installments for new connections for Urban poor Water and Energy Data of Hubli-Dharwad Water Supply System Energy Efficiency Measures implemented in 8/2004 Sl.No. Details Before 8/2004 (From 7/2003 to 6/2004) 1 Volume pumped from Reservoir / annum 22667 ML 2 Total energy use at Soundatti & Amminbhavi of Malprabha WSS (Million Kwh) 31.93 Million Kwh After 8/2004 (From 10/2004 to 9/2012) Period Data (From 10/2004 to 9/2005) 28666 2005 29.89 2005 2.0407 Million Kwh 2006 28.67 2006 3.2584 Million Kwh 2007 25.63 2007 6.2584 Million Kwh 2008 23.94 2008 7.9941 Million Kwh 2009 22.71 2009 9.2241 Million Kwh 2010 22.56 2010 9.37 Million Kwh 2011 27.73 2011 4.20 Million Kwh Total Energy saving 3 Total Energy Cost / annum ` 11.45 Crore Results Achieved Period Data Increase in Flow by about 25% (2005-09) 28.82 Million Kwh 2005 10.60 2005 ` 0.85 Crores 2006 10.15 2006 ` 1.30 Crores 2007 9.15 2007 ` 2.05 Crores 2008 8.59 2008 ` 2.86 Crores 2009 8.19 2009 ` 3.26 Crores 2010 9.00 2010 ` 2.45 Crores 2011 11.06 2011 ` 0.39 Crores Saving of Energy Cost (2005-11) ` 13.16 Crores INCREASE IN COST RECOVERY Amount in Rs Millions Year Revenue Power Charges M&R Cost O&M Cost Capital Works Dept service Full Cost O&M Ratio FCR Ratio 2001-02 34.50 87.20 144.00 231.20 31.10 30.00 292.30 6.70 8.47 2002-03 36.10 114.60 108.50 223.10 23.40 35.00 281.50 6.18 7.80 2003-04 44.12 153.34 91.74 245.08 16.54 40.00 301.63 5.56 6.84 2004-05 59.95 146.27 117.78 264.05 19.57 56.93 340.55 4.40 5.68 2005-06 105.18 182.22 101.33 283.55 23.85 50.00 357.40 2.70 3.40 2006-07 119.80 179.78 120.62 300.40 26.03 46.29 372.72 2.51 3.11 2007-08 158.44 173.67 127.79 301.46 18.74 52.08 372.27 1.90 2.35 2008-09 157.37 138.31 157.58 295.89 34.93 61.48 392.30 1.88 2.49 2009-10 165.98 132.63 161.50 294.13 34.60 46.65 375.38 1.77 2.26 2010-11 179.61 155.26 185.43 340.69 26.04 78.29 445.02 1.90 2.48 2011-12 293.19 202.90 194.41 397.31 24.29 79.09 500.69 1.36 1.71 2012-13 267.29 234.82 158.96 393.78 49.87 117.88 561.53 1.47 2.10 National Urban Water Award 2009 at New Delhi on 11-08-09 for IMPROVING WATER SERVICES THROUGH FINANCIAL REFORMS IN HUBLI-DHARWAD Thank you BASICS OF BIOLOGICAL WASTEWATER TREATMENT Dr. K.S. LOKESH Professor & Head Department of Environmental Engineering S J College of Engineering (Autonomous) Mysuru 570 006 E-mail: lokeshkaggere@yahoo.com PRESENTATION OUTLINE WASTEWATER SCENARIO OF INDIA REACTION KINETICS, UNIT OPERATIONS & UNIT PROCESSES MICROBIAL REACTION KINETICS REACTOR, REACTOR SYSTEMS & APPLICATIONS PRINCIPLE OF MASS BALANCE & ITS APPLICATIONS TREATMENT TYPES & ACTIVATED SLUDGE PROCESS & DESIGN CONSIDERATIONS BIOKINETIC COEFFICIENTS & ASP’s MODIFICATIONS SUMMING UP WASTEWATER TREATMENT • IMPORTANCE AFTER LATE 17OOs • 1780:INVENTION OF MICROORGANISMS • BOTH WATER TREATMENT AND SEWAGE (WASTEWATER) TREATMENT HAVE SEEN REMARKABLE SHIFT IN TREATMENT PROCESSES DOMESTIC WASTEWATER – INDIAN SCENARIO 2011 DEER ISLAND WASTEWATER TREATMENT PLANT, USA BASIC CONSIDERATIONS • REACTION KINETICS • UNIT OPERATIONS & UNIT PROCESSES • REACTORS AND REACTOR SYSTEMS • FUNDAMENTAL PRINCIPLE OF MASS BALANCE • MICROBIAL REACTION KINETICS • BIOKINETIC COEFFICIENTS • DESIGN CONSIDERATIONS SIMPLE REACTION (A B) ORDER OF REACTION • IN CHEMICAL KINETICS, THE ORDER OF REACTION WITH RESPECT TO A GIVEN SUBSTANCE (SUCH AS REACTANT, CATALYST OR PRODUCT) IS DEFINED AS THE INDEX, OR EXPONENT, TO WHICH ITS CONCENTRATION TERM IN THE RATE EQUATION IS RAISED • FOR THE TYPICAL RATE EQUATION OF FORM : • r = K AX BY WHERE [A], [B], ... ARE CONCENTRATIONS, THE REACTION ORDERS (OR PARTIAL) ARE X FOR SUBSTANCE A, Y FOR SUBSTANCE B, ETC. • THE OVERALL REACTION ORDER IS THE SUM X + Y + HALF LIFE • THE HALF-LIFE OF A REACTION, T1/2, IS THE AMOUNT OF TIME NEEDED FOR A REACTANT CONCENTRATION TO DECREASE BY HALF COMPARED TO ITS INITIAL CONCENTRATION • ITS APPLICATION IS USED IN CHEMISTRY AND MEDICINE TO PREDICT THE CONCENTRATION OF A SUBSTANCE OVER TIME SIGNIFICANCE OF HALF LIFE ZERO ORDER REACTION • A ZERO-ORDER REACTION IS A REACTION THAT PROCEEDS AT A RATE THAT IS INDEPENDENT OF REACTANT CONCENTRATION • TYPICALLY WITH INCREASING OR DECREASING REACTANTS CONCENTRATIONS NOT AFFECTING THE OBSERVED REACTION • THIS MEANS THAT THE RATE OF THE REACTION IS EQUAL TO THE RATE CONSTANT, K, OF THAT REACTION • THIS PROPERTY DIFFERS FROM BOTH FIRSTORDER REACTIONS AND SECOND-ORDER REACTIONS ZERO ORDER PLOTS FOR CONCENTRATION & RATE V/S TIME ZERO ORDER REACTION DIFFERENTIAL RATE EQUATIONS - dc/dt= r = k INTEGRATED RATE EQUATIONS (Ct) = -kt + (C0) HALF LIFE EQUATION t 1/2= (C0) / 2k FIRST ORDER REACTION • A FIRST-ORDER REACTION IS A REACTION THAT PROCEEDS AT A RATE THAT DEPENDS LINEARLY ONLY ON ONE REACTANT'S CONCENTRATION FIRST ORDER PLOTS FOR CONCENTRATION & RATE V/S TIME FIRST ORDER REACTION DIFFERENTIAL RATE EQUATIONS - dc/dt = k (C) --- INTEGRATED RATE EQUATIONS ln (C) = -kt + ln (C0) C = C0 e-kt Exponential Decay Equation HALF LIFE EQUATION t 1/2= ln (2) /k ---- SECOND ORDER REACTION • A REACTION IS SAID TO BE SECOND ORDER WHEN THE OVERALL ORDER IS TWO • THE RATE OF A SECOND-ORDER REACTION MAY BE PROPORTIONAL TO ONE CONCENTRATION SQUARED, OR (MORE COMMONLY) TO THE PRODUCT OF TWO CONCENTRATIONS SECOND ORDER REACTION DIFFERENTIAL RATE EQUATIONS - dc/dt = 2k (C1)2 INTEGRATED RATE EQUATIONS 1/C = 1/C0 + k t - dc/dt = k (C1) (C2) C1/C2 = C1/C2 e(C1-C2) k t HALF LIFE EQUATION t 1/2= 1/k(C1) lnr = ln k + 2 ln (C1) Where C1 is not equal to C2 - dc/dt = 2k (C1)2 ---- ---- ---- ---- ---- RATE EQUATIONS nth ORDER REACTION DIFFERENTIAL RATE EQUATIONS INTEGRATED RATE EQUATIONS - dc/dt = k (C)n 1/Cn-1 = 1/C0n-1 + (n-1) kt HALF LIFE EQUATION t ½= 2n-1 /(n-1)k(C0)n-1 HALF LIFE REACTION RATE WASTEWATER TREATMENT UNIT OPERATIONS • PHYSICAL FORCES DOMINATE EX : FLOATATION, EVAPORATION, SEDIMENTATION, FILTRATION, AERATION, COMMINUTOR UNIT PROCESSES • CHEMICAL AND BIOCHEMICAL REACTIONS DOMINATE EX : DISINFECTION, COAGULATION, ADSORPTION, CHEMICAL PRECIPITATION, BIODEGRADATION TREATMENT TYPES • PRILIMINARY (SCREENS, GRIT CHAMBER) • PRIMARY (COMMINUTOR, GRIT CHAMBER, PST) • SECONDARY / BIOLOGICAL (ASP, TF, BIOTOWERS, BIOMEMBRANES) • TERTIARY (COMBINATION OF CHEMICAL & BIOCEHMICAL PROCESSES) • QUATERNARY / ADVANCED (REMOVAL OF REFRACTORY ORGANICS, RESIDUAL SOLIDS, TOXIC ELEMENTS, GASES ETC.,) TYPICAL WASTEWATER TREATMENT FLOW DIA REACTORS (TREATMENT UNITS) • COMPLETELY MIXED BATCH REACTOR (CMBR) • CONTINUOUS FLOW STIRRED TANK REACTOR (CFSTR) • PLUG FLOW REACTOR (PFR) • COMPACT BED REACTOR (CBR) • FLUIDIZED BED REACTOR (FBR) • HYBRID REACTORS (UASB, SBR, MBR ETC.,) COMPLETE – MIX BATCH REACTOR (CMBR) • FLOW NEITHER ENTERS NOR LEAVES THE REACTOR • THE LIQUID CONTENTS OF THE REACTOR ARE MIXED COMPLETELY COMPLETE – MIX REACTOR (CFSTR) • ASSUMED COMPLETE MIXING OCCURS INSTANTANEOUSLY AND UNIFORMLY THROUGHT THE REACTOR • THERE WILL BE CONTINUOUS INFLOW AND OUTFLOW • SOME CHANGE IS EXPECTED TO TAKE PLACE WITHIN THE VOLUME OF THE REACTOR PLUG FLOW REACTOR (PFR) OPEN CLOSED • LITTLE OR NO LONGITUDINAL MIXING • LONGITUDINAL DISPERSION IS MINIMAL OR ABSENT • PARTICLES REMAIN IN THE REACTOR RETAINING THEIR IDENTITY IN THE REACTOR FOR A TIME EQUAL TO THEORETICAL DETENTION TIME CFSTRs’ IN SERIES IDEAL PLUG FLOW REGIME PREVAILS PACKED BED REACTOR • PACKED WITH SOME TYPE OF MATERIAL • CAN BE UPFLOW OR DOWN FLOW • DOSING CAN BE CONTINUOUS OR INTERMITTENT • CAN BE ARRANGED IN STAGES FLUIDIZED BED REACTOR • SIMILAR TO THAT OF PACKED BED REACTOR, BUT THE BED IS EXPANDED BY UPWARD MOVEMENT OF FLUID • FLOW RATE CONTROLS THE EXPANDED BED POROSITY APPLICATIONS OF REACTORS SL. NO. REACTOR TYPE ENGINEERING APPLICATIONS 1. BATCH REACTOR SBR, MIXING OF SOLUTIONS 2. COMPLETE MIX & WITH RECYCLE AERATED LAGOONS, AEROBIC SLUDGE DIGESTION, ASP 3. PLUG FLOW & WITH RECYCLE CHLORINE CONTACT BASIN, NATURAL TREATMENT SYSTEMS, ASP, AQUATIC TREATMENT SYSTEMS 4. COMPLETE MIX REACTORS IN SERIES LAGOON TREATMENT SYSTEMS, USED TO SIMULATE NON-IDEAL FLOW IN PLUG FLOW REACTORS 5. PACKED BED AIR STRIPPING, TRICKLING FILTERS, DEPTH FILTERS, NATURAL TREATMENT SYSTEMS 6. FLUIDIZED BED AIR STRIPPING, UASB, AEROBIC & ANAEROBIC TREATMENT SYSTEMS MASS BALANCE • A MASS BALANCE, ALSO CALLED A MATERIAL BALANCE, IS AN APPLICATION OF CONSERVATION OF MASS TO THE ANALYSIS OF PHYSICAL SYSTEMS • BY ACCOUNTING FOR MATERIAL ENTERING AND LEAVING A SYSTEM, MASS FLOWS CAN BE IDENTIFIED WHICH MIGHT HAVE BEEN UNKNOWN, OR DIFFICULT TO MEASURE WITHOUT THIS TECHNIQUE • THAT MATTER CANNOT DISAPPEAR OR BE CREATED SPONTANEOUSLY MASS BALANCE - DEFINITION • INPUT = OUTPUT + ACCUMULATION • INPUT + GENERATION = OUTPUT + ACCUMULATION + CONSUMPTION DEFINITION SKETCH V C SYSTEM BOUNDARY CONTROL VOLUME BOUNDARY MASS BALANCE APPROACH • MASS IS NEITHER BE CREATED NOR BE DESTROYED, BUT THE MASS CAN BE ALTERED • DEFINES THE RATE OF CHANGE OF MASS AS A FUNCTION OF TIME • HAS A WELL DEFINED SYSTEM BOUNDARY MASS BALANCE APPROACH • SYSTEM BOUNDARY IDENTIFIES FLOWS INTO AND OUT OF THE SYSTEM • CONTROL VOLUME IS TO IDENTIFY THE ACTUAL VOLUME IN WHICH CHANGE IS OCCURING • MOST OF THE CASES BOTH OF THEM COINCIDE ASSUMPTIONS • THE VOLUMETRIC FLOW INTO AND OUT OF THE REACTOR VOLUME IS CONSTANT (STEADY STATE / EQUILIBRIUM CONDITION) • THE LIQUID WITHIN THE CONTROL VOLUME IS MIXED COMPLETELY • THE LIQUID WITHIN THE CONTROL VOLUME IS NOT SUBJECT TO EVAPORATION • CHEMICAL REACTION INVOLVING A REACTANT IS OCCURING WITHIN THE REACTOR • THE RATE OF CHANGE OF REACTION IS GOVERNED BY FIRST ORDER REACTION KINETICS (rc = - kC) GENERAL MASS BALANCE ANALYSIS SIMPLIFIED WORD STATEMENT • ACCUMULATION = INFLOW – OUTFLOW + GENERATION SYMBOLIC REPRESENTATION • dc / dt x V = QC0 – QC + rc V Substituting –kC for rc GENERAL MASS BALANCE ANALYSIS • dC/dt x V = QC0 – QC + (-kC) V dc/dt = rate of change of reactant concentration within the control volume, ML-3T-1 V = Volume contained within the control volume , L3 Q = Volumetric flow rare into and out of reactor, L3T-1 Co = Concentration of reactant entering the control volume, ML-3 C = Concentration of reactant leaving the control volume, ML-3 rc = First order reaction (- kC) , ML3T-1 k = First order reaction rate coefficient, T-1 DIMENSIONAL ANALYSIS (UNITS’ CHECK) • UNITS OF INDIVIDUAL QUANTITIES MUST BE CONSISTENT • V = m3 , dc/dt = g/m3 s , Q = m3/s , Co, C = g/m3 , k = L/s • g/m3 s x m3 = m3/s (g/m3 ) - m3/s (g/m3 ) + (-1/s) (g/m3 ) m3 • g/s = g/s – g/s – g/s HENCE, THE UNITS ARE CONSISTENT BACTERIAL GROWTH CURVE MONOD’S KINETICS BIOKINETIC COEFFICIENTS COEFFICIENT UNIT VALUE kg BOD / kg MLVSS.d 0.2 - 0.4 kg BOD / m3.d 0.3 - 0.7 DAYS 3 - 15 k g COD / g VSS.d 2 - 10 Ks mg / L BOD 25 -100 Y mg VSS / mg BOD or COD kd g VSS / g VSS.d F/M LOADING MCRT (BSRT) 0.4 - 0.8 & 0.3 - 0.6 0.06 - 0.15 SECONDARY (BIOLOGICAL) TREATMENT 1. AEROBIC SYSTEM - SUSPENDED & ATTACHED 2. ANEAROBIC SYSTEM - SUSPENDED & ATTACHED 3. ANOXIC SYSTEM 4. FACULTATIVE SYSTEM ACTIVATED SLUDGE PROCESS (ASP) • AN ACTIVE SYSTEM WHERE MICROBES ARE KEPT ACTIVE THROUGH SUPPLY OF OXYGEN, FOOD AND CONDUCIVE ENVIRONMENT • ALWLAYS MAINTAINS AEROBIC CONDITION • PRODUCES BIOMASS (BIOSLUDGE) • CONTINUOUS TREATMENT SYSTEM TYPICAL ACTIVATED SLUDGE PROCESS ASP MODIFICATIONS SL. No. 1. MODIFICATION ADVANTAGE TAPERED AERATION REDUCED OXYGEN LOAD AT THE END OF THE TANK 2. STEP AERATION MORE UNIFORM OXYGEN DISTRIBUTION 3. COMPLETELY MIXED COMMON & PROVEN PROCESS 4. CONTACT STABILIZATION SMALLER AERATION VOLUME 5. EXTENDED AERATION HIGH QUALITY EFFLUENT 6. OXIDATION DITCH HIGHLY RELIABLE, ECONOMIC & SIMPLE 7. PURE OXYGENATION SMALL AERATION TANK VOLUME AERATION SYSTEMS IN ASP DESIGN CONSIDERATIONS • MASS BALANCE APPROACH • BASIC ASSUMPTIONS • MONOD’S REACTION KINETICS • SUBSTRATE LOADING & HYDRAULIC LOADING RATES • SUBSTRATE UTILIZATION • MICROBIAL GROWTH RATE GLOBAL OUTLOOK (Source : UN & WB, 2006) PERCENTAGE OF WORLD’S DEVELOPED COUNTRIES DEVELOPING COUNTRIES POPULATION 19 81 POPULATION GROWTH 0.1 1.5 WEALTH & INCOME 85 15 RESOURCE USE 88 12 POLLUTION & WASTE 75 25 SUSTAINABLE DEVELOPMENT “ DEVELOPMENT THAT MEETS THE NEEDS OF THE PRESENT WITHOUT COMPROMISING THE ABILITY OF FUTURE GENERATIONS TO MEET THEIR OWN NEEDS" The World Commission on Environment and Development INFLUENCING FACTORS • ECONOMY • ECOLOGY • CULTURE • POLITICS SUSTAINABILITY LOOP SERVICES EQUITY BIODIVERSITY HOUSE HOLD NEEDS PARTICIPATION NATURAL RESOURCES INDUSTRIAL GROWTH EMPOWERMENT CARRYING CAPACITY AGRICULTURAL GROWTH SOCIAL MOBILITY ECOSYSTEM INTEGRITY EFFICIENT USE OF LABOUR CULTURAL PRESERVATION CLEAN AIR AND WATER PRINCIPLE OF ENVIRONMENTAL SUSTAINABILITY CONSUMPTION OF RENEWABLE RESOURCES STATE OF ENVIRONMENT SUSTAINABILITY More than Environmental nature's ability to degradation replenish Not sustainable Equal to nature's Environmental ability to equilibrium replenish Steady State Economy Less than Environmental nature's ability to renewal replenish Environmentally sustainable PATH TO SUSTAINABILITY NATURAL CAPITAL NATURAL CAPITAL DEGRADATION SOLUTIONS TRADE - OFFS INDIVIDUALS MATTER SUMMING UP • BASIC CONSIDERATIONS • REACTION KINETICS & MASS BALANCE • REACTORS AND THEIR APPLICATIONS • MICROBIAL GROWTH KINETICS • BIOKIENTIC COEFFICIENTS • BIOLOGICAL WASTEWATER TREATMENT – ACTIVATED SLUDGE PROCESS • DESIGN CONSIDERATIONS