mbr-c1 fundamentals of mbr

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  • 7/21/2019 MBR-C1 Fundamentals of MBR

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    MBR CourseFundamental of MBR Processes &Introduction to Process Design Tools

    October 16 & 17, 2012

    Hamid Rabie

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    Function of a WWTP

    Removal of particulate materials

    sand hairs, fibrous materials

    other solids

    Biodegradation of undesired components

    Solid liquid separation

    WWTPEffluent

    Surplus sludge (biomass)

    Wastewater

    phosphorus biomass

    carbon

    nitrogen

    sulphur

    CO2 + biomassN2 + biomass

    biomass

    Microbial rejection

    biomass rejection

    standard sedimentation: 10,000 CFU/ml(colony forming unit: cfu)

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    Solid - Liquid

    Separation

    Biological Process

    Fundamentals of Bio-Reactor Processes

    Wastewater Effluent

    SludgeEngineered systems to:

    Accumulate microorganisms for oxidation of electron donor pollutants.

    Convert soluble pollutants to large particles (biomass) for separation.

    Settling Filter media Membrane

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    Fundamentals of Bio-Reactor Processes

    Aerobic

    Anoxic Aerobic

    Anaerobic Anoxic Aerobic

    Pollutant Measurement Biological Reaction Process Name Condition

    Carbonaceous BOD, COD cellsCOOrganic O

    + 22 BOD Removal Aerobic

    Ammonia N - NH3 cellsNONH O + 332 Nitrification Aerobic

    Nitrate TNcellsNNO

    +

    23

    Denitrification Anoxic

    Phosphorous TP cellsP Bio-P Removal Anaerobic

    BOD / Nit

    BOD / Nit / Denit

    BOD / Nit / Denit

    Bio-P

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    First Use of Membranes in Biological WWT

    SGFPCBS

    = Step screen= Grid and fat removal= Primary clarifier= Biological step

    STDCMT

    = Sedimentation tank= Third cleaning step (e.g. filtration)= Membrane technology

    Effluent treatment with membrane technology tertiary treatment

    Raw

    wastewater

    Effluent

    S GF PC ST DCBS MT Permeate

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    Membranes at the End of WWT Process

    Always end of the processes

    Tertiary treatment

    Almost similar to surface water treatment (need for coagulant)

    Low solid concentrationtolerance in membrane stage

    Mostly dead end filtration mode

    Sensitive against foulingcomponents

    Interesting for existing WWTP that need disinfection or reuse

    additional costs to conventional technology;additional footprint required

    no hair and fibrous material allowedrequires easy sludge management

    Pressurized membrane systems or

    Submerged membrane systems

    fouling components come in direct contactwith membrane surfaces;often additional flocculation required;operation difficult to optimize

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    Raw

    wastewater

    S

    Effluent

    TCPC BS STGF

    Changes in the MBR System

    S

    GFFSBS

    = Step screen

    = Grid and fat removal= Fine screen= Biological step

    MT = Membrane technology

    Membrane bioreactor (MBR)

    BSFS MT

    Permeate

    Combination ofbiological stepand solid liquidseparation

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    MBR vs. Conventional Activated Sludge

    Pre-TreatmentIncomingWastewater Effluent

    AnoxicZone

    AerobicZone

    SettlingTank

    RAS

    Conventional Activated Sludge SystemConventional Activated Sludge System

    Pre-TreatmentIncomingWastewater

    AnoxicZone

    AerobicZone

    RAS

    Membrane Bioreactor (MBR)Membrane Bioreactor (MBR)

    EffluentMF/UF

    In case of TertiaryMore processes;

    e.g. sand filter

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    MBR Reduces the Footprint

    Membranes

    Eliminate all clarifiers

    Replace withmembrane systems

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    Major Differentiations of MBR Technology

    Activated

    SludgeProcess

    Membrane

    FiltrationMBR

    Stable

    Biological

    Treatment

    Process

    Absolute

    SolidsSeparation

    Replaces conventional clarification; requires less footprint

    Combines physical barrier of a membrane with biological treatment

    Produces high quality effluent at all times Comparable to tertiary treatment; then LCC is conventional technologies

    membranekey component to this market

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    Better effluent quality> 95%, 98% and 99.9% for COD,BOD, SS removal

    Effluent TSS independent of

    bioreactor efficiency

    High MW organics are retained andbio-degraded

    Improved biological reactions (dueto longer SRT, shear, etc.)

    Process ControlComplete separation between HRTand SRT

    Accurate control over sludge age,development of slow-growing

    microorganisms (nitrifiers)

    Increased EfficiencyAll bacteria retained, cold weathernitrification

    Insoluble P retained reducing

    chemical addition for P removal

    High MLSS (1-2%), greater organicloads and less sludge production

    Compact systems, less footprint

    Sludge digestion within bioreactor

    Modular expansion

    Absorbs variation and fluctuations inincoming flow and organic loads

    Advantages of MBR over Conventional

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    Market Areas for MBR Technology

    MembraneBioreactors

    leachate

    municipalwastewater textile

    industry

    industriallaundries

    pulp &paper

    tank

    cleaning

    beverageindustry

    dairyindustry

    vegetableindustry

    fruitindustry

    Slaughter-house /

    rendering

    petrochemindustry

    chemicalindustry

    pharmacy

    industry

    High ammoniacontent

    High CODcontent

    High CODcontent

    High & variablesalt content

    Space limitation

    reuse; high quality

    High &variable salt

    content

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    Increasing regulatory standards

    especially regarding disinfectant by-

    products and waterborne pathogens

    Limited supply

    tap into alternative supplies

    such as water re-use

    Growing demand

    due to population growth, newinfrastructure in developed

    countries, and aging infrastructure

    in industrialized countries

    Technological innovation

    development of low cost,

    high quality water treatment

    solutions

    Growth inMembrane

    Technology

    Drivers of MBR Market & Technology

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    Hollow fiber modules Plate modules

    GE-Zenon

    Mitsubishi

    Siemens-Memcor

    Koch Membrane-Puron

    Micronet PF

    Kubota

    Toray

    Huber

    A3 Gmbh

    Tubular modules

    Outside/In FiltrationImmersed (Vacuum)

    Outside/In FiltrationImmersed (Vacuum)

    Inside/Out Filtration(Pressurized Vessel)

    Main Configurations for MBR Technology

    X-Flow / Pentair

    Berghof

    Koch Membrane

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    modules cross flow operation

    MBR with Tubular Modules -Cross Flow Membrane Filtration

    External cross flow MBR

    RCRL

    MFDN N

    RCRL

    MFNDN

    recirculationreturn line

    membrane filterNitrificationDe-nitrification

    PressurePump

    Module Length

    Pressure

    Feed side

    Permeate side

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    Cross Flow Membrane Filtration for MBR Tubular Membrane (Inside/Out Filtration)

    Membrane

    Support Material

    Feed

    (Clean Water)

    Permeate

    Concentrated

    Waste

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    Cross Flow Membrane Filtration for MBR Tubular Membrane

    Original work-horse in MBR applications; used horizontal configuration

    Large diameter membrane tube and high recirculation flow rate and high

    TMP served to eliminate potential for plugging with biomass Membrane designed to operate at MLVSS levels > 50,000 mg/l

    Energy intensive on large flow rates (> 300,000 gpd)

    Low packing density (requires large footprint for large flow rates) New tubular systems from X-Flow uses air plugs in vertical tubes

    operating at lower pressures

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    Tubular MBR Configurations

    MLSS: 12-50 g/L

    Flux: 50-150 lmh

    High energy consumption:

    (1.5-4.0 kWh/m3)

    Continuous

    TMP: 1.0-5.0 bar

    MLSS: 8.0-12 g/L

    Flux: 30-50 lmh

    Lower energy consumption:

    (0.3-1.0 kWh/m3)

    Discontinuous

    TMP: 0.2-0.6 bar

    More valves & complexity

    X-Flow Airlift

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    Waste water

    Air

    MBR with Submerged (Immersed) membranes

    Biological sludge

    Vacuum Pump

    Permeate

    submergedmembranes

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    Basic of Immersed MBR Train

    1.Biological reactor

    2.Membranes

    3.Permeate pump & blower

    4. Control panel

    5. Permeate & air piping

    1

    2

    43

    5

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    Immersed Membrane Filtration (hollow fiber)

    Membrane

    Coarse Bubble

    Diffuser

    Permeate to Top Header

    (Puron has no top header)Support Material

    (e.g. Zenon, MPF, Puron)

    Permeate to Bottom Header(Siemens has no bottom header)

    Bulk Fluid

    (Concentrate)

    Aeration

    Bubbles (forfluid agitation)

    Coarse Bubble

    Diffuser

    Outside/In Filtration

    S

    uction

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    Immersed Hollow Fibers in Operation

    Module Installationwith crane

    Submerged module in operationair injection phase

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    Immersed Membrane Filtration (flat sheet)

    Air bubbles between

    membrane panelsAir diffusers

    Suction

    To suction

    Panel

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    MBR with submerged modules -different tank configurations

    Internal submerged MBR

    RC

    MFDN N

    RCRL

    MFNDN

    recirculationreturn line

    membrane filterNitrificationdnitrification

    External submerged MBR (Preferred)

    RCRL

    DN N MF

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    Key Aspects of MBR Products

    Membrane structure and characteristics

    For superior technological and economical performance, should consider:

    Module design and features

    Membrane tank hydraulics

    Membrane filtration process and system design

    Aeration system & sludge management

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    Classification of membrane processes

    Nano-filtration

    RO

    1

    10

    100

    Pressuredifference

    in

    [bar]

    VirusesBacteria

    Saline solutions

    0,1

    Particle size in [m]

    0,1 1,0 10,00,010,0010,0001 100

    Sandfiltration

    Microfiltration

    Ultrafiltration

    Membrane pore size range from

    different suppliers for MBR

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    Comparison of microorganisms vsmembrane pore size

    poresize ~ 0,01 m

    ultrafiltration

    poresize ~ 0,2 m

    microfiltration

    E. Coli ~ 0,5 - 1,5 m

    MS2-Virus (Coliphage)

    ~ 0,025 m

    B. Subtilis~ 0,3 m

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    MBR provides better effluent quality

    Parameter MBRconvent.

    plant

    Solids mg/l 0 10 15

    COD mg/l < 30 40 50

    Ptotal withprecipitation

    mg/l < 0,3 0,8 1,0

    MLSS content inaeration tank

    g/l < 20 < 5

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    Key Requirements for Membrane Properties

    hydrophilicity - good wetability with water

    low fouling tendency

    chemical and thermal stability

    Material requirements

    mechanical stability

    narrow pore distribution

    minimized number of defects

    high porosity

    low hydraulic resistance

    high bonding of membrane to support material

    Morphological requirements

    cost-effective materials

    cost-effective production

    Economic requirements

    Diff t T f M b & St t

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    Different Types of Membranes & Structures(SEM of Membrane Surfaces)

    Mitsubishi

    2 m2 m

    KubotaToray

    3 m2 m

    Zenon

    Avg. Pore: 0.03 m

    PVDF low MW

    Asymmetric

    Coated on a support

    Avg. Pore: 0.1 m

    PVDF high MW

    Asymmetric

    Coated on fabric

    Avg. Pore: 0.4 m

    Chlorinated PE

    Symmetric

    Coated on fabric

    Avg. Pore: 0.2 m

    PVDF low MW

    Asymmetric

    Double coating

    Coated on support10 m

    Asymmetric Structure

    Membrane Skin/Surface

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    Introduction to DesignTools

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    Key Elements of MBR Process Design

    Full step by step biological reaction analysis and mass balances such as:

    Carbon, Phosphorous, Nitrogen, etc

    Sludge production

    Aeration and nutrient requirements

    Step by step process mass balances and all necessary sizing such as:

    Pumping and coarse screen

    Sand and fat removal Fine screen

    Equalization

    All dosing systems

    Different biological steps

    Sludge treatment

    Membrane systems: filtration tank, configuration, RAS, sludge g=feed,aeration capacity, blower sizes, pump sizes, chemical dosing, etc

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    System Configuration

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    Step by Step Process Calculations

    S b S P C l l i

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    Step by Step Process Calculations

    Process Trends for Different Key Parameters

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    Process Trends for Different Key Parameters