wastewater reuse tech evolution costs

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    Wastewater recycle and reuse:

    The need of the hour Workshop

    Date: 18 April 2012,

    Ministry of Urban Development, Govt. of India

    Uday G. Kelkar, Ph.D., P.E., BCEE

    NJS Consultants Co. Ltd., Japan

    Wastewater Recycle and Reuse

    Technology Evolution and Costs

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    Recycle and ReuseRecycle and Reuse

    -- Balancing ActBalancing Act

    Irrigation

    Secondary

    Treatment

    Restricted

    Urban Reuse

    TertiaryFiltration

    Industrial Non-Potable Reuse

    Indirect

    Potable Reuse

    Direct

    Potable or

    High QualityProcess

    Tertiary

    membrane

    Filtration

    N&P Control

    RO &

    Disinfection

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    Treatment AlternativesTreatment Alternatives

    Agricultural Reuse

    lowest water quality, lowest cost

    Conventional Secondary Treatment- No N & P

    Control

    highest water loss, drainage water has low

    quality

    Unrestricted Urban ReuseTertiary Filtration required

    Conventional

    Membranes Ultra or Micro filtration

    Disincection

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    Unit Operations inUnit Operations in

    Wastewater TreatmentWastewater TreatmentBiological

    Aerobic

    Process

    Anaerobic

    Process

    Suspended

    Growth

    Attached

    Growth

    Activated

    Sludge(ASP)

    CSTR, Plug flow, Sequencing Batch reactor,

    oxidation ditch, Orbal, Biolac, Cyclic ASP,Extended Aeration, aerobic/aerated lagoons

    Trickling Filter and Trickling

    filter with solids contact

    system

    SubmergedAttached

    Growth

    Rotating Biological

    Contactors (RBC)

    ASP with fixed film packing

    Down flow attached growth process, upflow

    submerged attached growth, fluidized bed

    bioreactor, membrane separation aerobic process

    Suspended

    Growth

    Attached

    Growth

    Anaerobic contact process, anaerobic sludge

    blanket process-UASB, anaerobic baffled

    reactor system,

    Up-flow packed bed attached growth, and

    expended bed reactors, anaerobic fluidized

    bed reactors, anaerobic lagoons, membrane

    separation anaerobic process

    Combination of aerobic and anaerobic process are used in tertiary treatment for

    the removal of nitrogen and phosphorus from the wastewater

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    NJS Consultants Co. Ltd

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    NJS Consultants Co. Ltd

    Surface Water DischargeSurface Water Discharge

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    Treatment AlternativesTreatment Alternatives

    Industrial ReuseTertiary Filtration and point-of-use treatment

    for higher water quality

    Nitrogen and Phosphorus control required

    like RO or EDR

    Disinfection

    Indirect Potable Reuse

    Filtration, MF/UF with RO

    Disinfection

    Need nitrogen and phosphorus removal

    Groundwater Recharge

    Need nitrogen removal

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    Technology selection criteriaTechnology selection criteria

    Reliable (proven and established)Reliable (proven and established)

    Recycled water quality and its consistencyRecycled water quality and its consistency

    Wastewater generation from treatmentWastewater generation from treatment

    processprocessOperator requirement / automationOperator requirement / automation

    Space requirement (may not be important forSpace requirement (may not be important forindustrial areas due to appropriate allocationindustrial areas due to appropriate allocation

    of land)of land)Capital cost, O&M cost (Lifecycle cost)Capital cost, O&M cost (Lifecycle cost)

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    ProcessSelectionMatrix

    D i M b P SiD i M b P Si

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    Decreasing Membrane Pore SizeSelectively Retains DifferentSubstances

    Decreasing Membrane Pore SizeSelectively Retains DifferentSubstances

    D

    ecreasing

    PoreSize

    Pure WaterPure Water

    Reverse Osmosis Membrane

    Nanofiltration Membrane

    Ultrafiltration Membrane

    Microfiltration Membrane

    Suspended solids Proteins Salts Bactena SugarSuspended solids Proteins Salts Bactena Sugar

    WaterWater

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    Tertiary filtration systemsTertiary filtration systems

    Raw

    Wastewater

    SecondaryEffluentActivatedSludge

    WAS

    Filters

    Sand filters Membrane filters

    Filtration size 40 microns 0.2 microns

    Outlet solids 5 10 mg/L < 2 mg/L

    Status in India Established Being considered

    Alum dosage High Medium

    STP outlet TP directly proportional to solids as

    biological and chemical processes convert soluble P intoparticulate P.

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    Recycle and Reuse

    - Balancing Act

    Irrigation

    Secondary

    Treatment

    Restricted

    Urban Reuse

    TertiaryFiltration

    Industrial Non-Potable Reuse

    Indirect

    Potable Reuse

    Direct

    Potable or

    High QualityProcess

    Tertiary

    membrane

    Filtration

    N&P Control

    RO &

    Disinfection

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    Dr Vinod Tare,

    IIT Kanpur

    April 24, 2010;IHC, New Delhi

    Workshop onSewage Treatment and Sludge Management

    Assessment of Technology for Sewage Treatment

    Criteria 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19

    Performance in terms of quality of treated sewage

    TSS, BOD, and COD

    Total / Faecal Coliform Removal

    DO in Effluent

    Initial/Immediate Oxygen Demand

    Nutrient Removal

    Performance ReliabilityImpact of Effluent Discharge

    Impact on Land

    Impact on Surface Waters

    Impact on Ground Waters

    1: Tech 1 ; 2: Tech 1 ; 3: Tech 1 ; 4: Tech 1 ; 5: Tech 1 ; 6: Tech 1 ; 7: Tech 1 ; 8: Tech 1 ; 9: Tech 1 ; 10: Tech 1 ; 11:

    Tech 1 ; 12: Tech 1 ; 13: Tech 1 ; 14: Tech 1 ; 15: Tech 1 ; 16: Tech 1 ; 17: Tech 1 ; 18: Tech 1 ; 19: Tech 1.

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    Dr Vinod Tare,

    IIT Kanpur

    April 24, 2010;IHC, New Delhi

    Workshop onSewage Treatment and Sludge Management

    Assessment of Technology for Sewage Treatment

    Criteria 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19

    Resource Generation

    Manure / Soil Conditioner

    Fuel

    Electricity Generation

    Food

    Impact of STP

    Impacts on Health of STP

    Staff/Locals

    Impacts on Surrounding

    Building/Properties

    Energy Requirement

    Land Requirement

    Capital Cost

    Recurring CostReinvestment Cost

    Level of Skill in O&M

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    WSP (Unlined)

    WSP (Lined)

    FAL

    TF (Plastic Media)

    TF (Gravel, Slow Rate)

    TF (Gravel, High Rate)

    UASB + FPU

    ASP

    UASB + FAL + FPU

    UASB + ASP

    BIOFOR

    ASP BIOFOR F

    FAB

    MBBR

    SBR / CTECH

    SAFF

    MBR

    ASP + C-F + RSF/DMF

    SBR + C-F + RSF/DMF

    Category I

    Category II

    Category III

    Category IV

    STPs Producing Recyclable Quality

    Treatment Plant Footprint, m2 / MLD

    0 2000 4000 6000 20000 25000 30000

    Annunali

    zedCost,Rs/kL

    0

    2

    4

    6

    8

    10

    Annualized Cost of Treatment and Corresponding Land

    Requirement for Various Treatment Technologies

    Adapted from Dr. Tare, 2010

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    Trends inTrends in Freshwater CostsFreshwater Costs

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    1995 2000 2005 2010 2015

    Year

    Lande

    dCostofwatertoUtility(Rsperk

    L)

    Chennai

    Delhi

    Hyderabad

    Bangalore

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    1995 2000 2005 2010 2015

    Year

    Lande

    dCostofwatertoUtility(Rsperk

    L)

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    Trends inTrends in Recycled Water CostRecycled Water Cost

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    1995 2000 2005 2010 2015

    Year

    Lande

    dCostofwatertoUtility(Rsperk

    L)

    Chennai

    Delhi

    Hyderabad

    Bangalore

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    1995 2000 2005 2010 2015

    Year

    Lande

    dCostofwatertoUtility(Rsperk

    L)

    MBR + RO (Potable)

    Tertiary treatment(All Non-potablescenario)

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    Growth in Indirect Potable ReuseGrowth in Indirect Potable Reuse

    0

    100,000

    200,000

    300,000

    400,000

    500,000

    600,000

    700,000

    800,000

    1960 1964 1969 1974 1979 1984 1989 1994 1999 2004

    C

    umulativeFlow,m

    3/d

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    Thank You!