anaerobic waste treatment

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    Anaerobic Waste Treatment

    What is anaerobic treatment?

    M&E: Biotreatment without oxygen. Bacteria that survive in anaerobic

    conditions are called obligate anaerobes.

    Typically:

    Organic waste carbon dioxide + methane

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    Advantages Over Aerobic Treatment

    1. low production of waste biological sludge- lower free energy release in organic waste conversion

    -slow biological growth, low solids production

    2. high degree of waste stabilization- aerobic: 85-90% BOD removal because of high biosolids, only

    - anaerobic: 85-95% BOD removal, 90% stable waste (CH4 not verysoluble in water so waste leaves system)

    3. lower nutrients required

    - operate at higher BOD, N:P ratios: P&P wastes often lacking inthese nutrients

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    Advantages Over Aerobic Treatment, cont.

    4. no O2 requirements- lower power requirements

    - reduced treatment costs- not limited by O2 transfer

    5. methane production

    - may be burned to generate heat

    or power

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    Soluble BOD

    1 kg

    Aerobic process

    CO2 + H2O

    0.5 kg

    New biomass

    0.5 kg

    Biode radable CODAnaerobic process

    CH4 gas

    > 0.9 kg

    1 kg

    New biomass

    < 0.1 kg

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    Disadvantages Over Aerobic Treatment

    1. optimum waste stabilization requires warm temperatures. Methanogens

    grow slowly (limiting factor)- mesophyllic: 35 - 38 (95 - 100)

    - thermophyllic: 58 - 60 (135 - 140)

    2. process is limited by slow biological (methanogenic) growth rates- requires longer startup period

    - m ts rate o process a ustment to c ang ng waste oa s, temp., etc.

    3. environmental sensitivity to O2, toxics, pH

    4. more favorable when applied to concentrated waste streams

    - BOD>10,000 mg/L

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    Process Description

    A. Conventional B. High-Rate(=30-60 days) (~15 days)

    InfluentInfluent

    Gas out(CH4 & CO2)

    (no mixing) (complete mix)

    supernatant

    active layer

    stabilized solids

    sludge sludge and supernatant to clarifier

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    Process Description, cont.

    C. Upflow anaerobic sludge blanket (UASB)

    D. Anaerobic contact process used on soluble BOD waste

    E. Fixed film anaerobic treatment process- anaerobic filter (fixed bed)

    - expanded or fluidized

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    Anaerobic Microbiology & Biochemistry

    Complexorganics

    Short-chainsolubleorganic

    monomers

    Organic acids:(acetic, proprionic,

    formic, etc.)

    CO2CH4

    acidformingbacteria

    methaneformingbacteriahydrolysis

    acetogenesis

    (waste conversion)

    methanogenesis

    (waste stabilization)

    Hydrolysis: cellulosic bacteria act on organic fibers to produce soluble organiccompounds (cellulose, lignins)

    Acetogenesis: acetogenic bacteria convert soluble organics to short-chain

    fatty acids (primarily acetic acid)

    Methanogenesis: Methanogenic bacteria convert organic acids to CH4 and

    CO2, most CH4 leaves the system

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    Common Volatile Acid Intermediates

    acetic acid: CH3COOH

    proprionic acid: CH3CH2COOH

    formic acid: HCOOH

    butyric acid: CH3CH2CH2COOH

    caprioc acid: CH3CH2CH2CH2CH2COOH

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    Methane Bacteria

    Methane bacteria

    - very sensitive to small concentrations of O2- slow growth rate- low rate of organic utilization

    Mechanism for methanogenesis

    * *- 3 4 2

    Reduction of CO2: CO2 + 8H CH4 + 2H2O

    Note: Microbiologists no longer consider methanogens to be in the bacterial domain. Recent RNAsequencing places methanogens in the domain Archaea. In fact, humans are more closelyrelated to cucumbers than methanogens are related to bacteria.

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    11

    th

    Ed. Brook Biology of Microorganisms

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    Methods of Predicting Methane Production

    422

    48248224

    :

    CHban

    COban

    OHba

    nOHC

    ncompositioWaste

    ban

    ++

    +

    +

    Prediction from waste stabilization:

    One pound UBOD or COD stabilized = 5.62 cubic feet CH4 (STP)

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    Waste Characteristics for Anaerobic Treatment

    organic strength (BOD, COD) + composition

    alkalinity

    pH (methanogenic range 6.8 7.4)

    inorganic nutrient content: BOD:N:P ratio

    temperature

    potentially toxic materials

    heavy metals

    ammonia common cations

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    Stimulatory/Inhibitory Effects

    from: Perry, 1964

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    Stimulatory and Inhibitory Concentrations(mg/L)

    Stim. Mod. Inhibit. Strong Inhibit.

    Sodium 100 - 200 3500 - 5500 8000

    Calcium 100 - 200 2500 - 4500 8000

    Magnesium 75 - 100 1000 - 1500 3000

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    Effect of Ammonia Nitrogen on Anaerobic Treatment

    Ammonia

    NitrogenConcentration

    (mg/L)

    Effect on

    AnaerobicTreatment

    50 200 Beneficial

    200 1000 No adverse effect

    1500 3000 Inhibitory athigher pH levels

    Above 3000 Toxic

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    Unbalanced Systems

    Indicators:

    volatile fatty acids (VFA) conc.: most important or utilized indicator

    pH (related to VFA, CO2

    CO2 in gas increasing

    total gas production decreasing

    waste treatment/stabilization decreasing

    Factors:

    temperature

    organic loading (waste strength)

    nature of waste