Waste Water Treatment

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Wastewater Treatment

description

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Transcript of Waste Water Treatment

  • Wastewater

    Treatment

  • Municipal WW Management Systems

    Sources of

    WastewaterProcessing at

    the SourceWastewater

    Collection

    Transmission

    and PumpingTreatment Reuse/Disposal

  • Sources & Types of WW

    Domestic Wastewater

    from residences, commercial & institutional

    flows ~70-90% of water supplied

    Industrial Wastewater

    highly dependent on industry

    Infliltration/Inflow

    enters through leaks, foundation drains, etc.

    Stormwater

    for combined sewers - largely in older cities

  • Typical WW Characteristics

    Parameter Conc.BOD 250 mg/L

    TSS 250 mg/L

    COD 500 mg/L

    Ammonia 30 mg/L

    TOC 100 mg/L

    Chloride + 50 mg/L

  • 1972: Federal Water Pollution Control Act

    PL 92-500 subsequently amended and now

    called the Clean Water Act

    established water quality goals fishable &

    swimmable and timetable

    established National Pollution Discharge

    Elimination System (NPDES)

    construction grants for WW treatment

    required secondary treatment (30/30)

    30 mg/L BOD5

    30 mg/L TSS

  • Conventional WW Treatment

    Biological ProcessPreliminary

    Treatment

    Secondary

    Sedimentation

    Sludge

    Disinfection

    Primary

    Sedimentation

    Sludge

  • Preliminary Treatment

    To remove materials that will interfere with

    subsequent treatment

    Coarse Screening (bar racks)

    Medium Screening

    Comminution

    Flow measuring

    Pumping

    Grit removal

    Pre-aeration

  • Bar Racks

    Metal bars spaced a few cm apart across

    water flow

    mechanical or manually cleaned

    size of unit set by approach velocity

    0.6-1.0 m/s for mechanically cleaned

    0.3-0.7 m/s for manually cleaned

    see Fig 10.4 and example 10.2 on pg. 311

  • Grit Removal

    Grit chambers intended to remove sand,

    cinders, gravel that may enter system by

    cracks in pipes, inflow etc.

    Grit can cause excess wear in pipes and

    pumps

    small sedimentation tanks; designed with

    the help of Stokes Law

    no organics removal

  • Grit Chamber

  • Primary Sedimentation

    Purpose: to remove suspended solids

    (smaller than grit, and less harmful)

    Typical efficiency

    67% TSS removal

    33% BOD removal

    Design parameters

    overflow rate

    weir loading rate

    detention time

    Primary effluent is

    largely composed of

    soluble and colloidal

    organics which can be

    converted to settleable

    microbial solids and

    CO2 by biological

    treatment

  • Primary Sedimentation Primary Treatment

    Removes ~50% of suspended solids

    Parameter Design Range Typical

    ValueOverflow

    Rate

    35-45 m/d

    800-1200 gal/ft2/d

    40 m/d

    1000 gal/ft2/d

    Detention

    Time

    1.5-2.5 h 2 h

    Weir loading

    rate

    125-500 m2/d

    10,000-40,000 gal/ft/d

    275 m2/d

    20,000 gal/ft/d

  • Primary Sed. Tank

  • Primary Clarifier: Center Feed

  • Secondary Treatment

    Generally includes some biological process

    plus secondary clarification

    Required under PL92-500

    Converts soluble and colloidal organic

    materials to biomass and CO2

  • Biological Treatment

    Suspended Growth

    Activated Sludge

    Conventional, Extended Aeration, Contact

    Stabilization

    Aerated lagoons

    Aerobic digestion

    Attached Growth

    Trickling Filters

    Rotating Biological Contactors

  • Suspended Growth Systems

    Sludge

    Secondary

    Sedimentation

    Return Activated Sludge

    Waste

    Activated Sludge

    Aeration Tank

    Air

  • Attached Growth: Trickling Filters

    Rocks or

    Plastic

    Media

    Underdrain

    Rotary Distributor

    With rocks, depth is limited to 2-3 m because of oxygen needs

    Air

  • Rotating Biological Contactors

    Drum diameters are typically 10-12 ft.

    Rotation speed: ~1.5 rpm

    May be in several stages

    No flow recycle

    Requires piloting

  • Secondary Clarifier

  • Sludge Disposal

    Thickening

    gravity, flotation

    Digestion

    aerobic, anaerobic

    Mechanical Dewatering

    Vacuum filtration, centrifugation, pressure filtr.

    Disposal

    land application, burial, incineration

  • Anaerobic Digestion

    Sludge held without aeration for 10-90 days

    Process can be accelerated by heating to 35-40oC

    These are called High Rate Digestors (10-20 days)

    Advantages

    low solids production

    useable methane gas produced

    Disadvantages

    high capital costs

    susceptibility to shocks and overloads

  • Sludge Dewatering

    Sludge drying beds

    historically the most common

    sand bed, 15-30 days, evaporation & seepage

    Vacuum Filtration

    cylindrical rotating drum covered with fabric

    submerged with applied vacuum

    Continuous belt filter presses (follows)

    Plate pressure filters

    vertical plates mounted on a frame

  • Belt Filter Press (Komline-Sanderson)