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Assessment and Disposal of Arsenic Treatment Residuals...SBRP/EPA Workshop Feb. 28 - Mar. 01, 2005 2...

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Assessment and Disposal of Arsenic Treatment Residuals SBRP/EPA Workshop Feb. 28 - Mar. 01, 2005
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  • Assessment and Disposal of

    Arsenic Treatment Residuals

    SBRP/EPA Workshop Feb. 28 - Mar. 01, 2005

  • 2 Philosophy and Format

    Road test research Proactive environmental engineering Condense normal timeline Cut across conventional delineations Limited size

    facilitate open discussion narrow focus/broad expertise solutions/directions beyond the problems

  • 3 Changes and Impacts

    •2001revised arsenic in D.W. standard •10 ppb MCL (from 50 ppb) •Implementation by 2006-2012

    •Predicted impacts •4000 new utilities impacted ( >95% small) •8M lb solid residuals annually (30,000 # As /yr) •Present and future Superfund/RCRA sites

    •Residuals hazard assessment •Toxicity characteristic leaching procedure (TCLP) •Waste extraction test (WET)

  • 4 Next Steps for As Residuals

    S1. Simulate landfills/repositories to determine appropriate performance bar

    S2. Develop tractable protocols based on engineering critical leaching mechanisms to clear bar

    S3. Evaluate (technically & economically) treatment options, including stabilization, alternative sorbents, etc.

    S4. Develop and evaluate hybrid (conventional & innovative) disposal options

  • 6 Test/Landfill Characteristics

    Test pH ORP (mV)

    Alkalinity (mg/L as CaCO3)

    TOC (mg/L)

    TDS (mg/L)

    Ionic Strength

    (M)

    TCLP 4.95 103.5 766 38.6 1480 0.08 WET 5.05 74 7940 55.8 5160 0.10 SL1 7.03 121.4 1500 1050 5200 0.03 SL2 7.55 -37 12500 1310 8600 0.49 LL1 6.82 36.1 1100 160 3600 0.33 LL2 4.5-9.0 N/R* 300-11500 30-29000 2000-60000 N/R LL3 6.5-8.2 N/R 1250-8050 N/R 1960-16800 N/R LL4 6.2-7.1 N/R N/R 236-3160 N/R N/R

    N/R* - Values Not Reported LL1 – Leachate collected from Tangerine Road Landfill, Tucson, AZ. LL2 – Leachate composition reported in Christensen et al, 2001 (21) LL3 – Leachate composition reported in Jang et al, 2003. (22) LL4 – Leachate composition reported in Hooper et al, 1998. (5)

  • 7 Our Corollary Research

    Treatment systems evaluation (IHS funding) Removal technology development (State of AZ/

    SBRP) Residuals assessment (SBRP/AZ State funding)

    Adequacy of TCLP and WET What is adequate? Alternative test development Other contaminants and scenarios

    Residuals stabilization (SBRP/AWWARF/AZ State funding)

  • 0

    0.2

    0.4

    0.6

    0.8

    1

    1.2

    Extra

    ctan

    t Ars

    enic

    (m

    g/L

    as A

    s)

    AA, 18hr AA, 48hr

    GFH, 18hr GFH, 48hr

    Initial Loading: AA, 31 ppb; GFH, 22 ppb

    TCLP LL WET SL1 SL2

    8 Solid Media Leaching

  • 9 Residuals Assessment Tests

    Guiding Premise: test induces leaching as or more aggressively

    than conditions of non-hazardous waste disposal

    TCLP WET Mature Landfill

    pH 4.95 5.05 7-9

    Bioactivity abiotic abiotic biotic

    Duration 18 hr 48hr weeks /months

    Active Reage nt

    acetate c itrate Mix of organics & inorganics

    Redox Condition

    oxidizing neutral reduc ing

  • 10 Immediate Findings

    •TCLP vs. WET Variables (batch test mode) •agitation method (tumbler (T) > shaker (W)) •headspace (N2 (W) > air (T)) •duration (48 hr (W) > 18 hr (T)) •reagent (citrate (W) > acetate (T))

    •Landfill vs. Standard Variables (batch test mode) •pH (6.8 (LL) > ~5 (T&W)) •TOC (above 160 ppm (LL) > below 60 ppm (T&W)) •ORP (below 50 mV (LL) > above 50 mV (T&W))

    •Study limitations •batch vs. continuous flow •abiotic vs. biotic •excess (non-reactive) vs. limiting (reactive) substrate

  • SYRINGE PUMP (FLOW RATE 0.31mL/min)

    INFLUENT GAS COLLECTION

    MARIOTTE

    FLASK

    10% NaOH SOLUTION

    UNSATURATED ZONE

    SATURATED ZONE

    GRAVEL

    GRAVEL

    WATER WITH pH LEVEL INDICATOR

    DEAERATED, COLLECTION DEIONIZED FLASK WATER

    SAMPLING PORTS • 23% SHREDDED PAPER • 46% YARD WASTE • 31% SOLID RESIDUAL • 4L ANAEROBIC DIGESTOR SLUDGE

    EFFLUENT

    11 S1. Setting the bar

    Landfill Simulation Columns

  • As

    (ppb

    ) 2500

    3000 3500

    4000 As(III)

    DMA(V)

    As(dissolved)

    MMA(V)

    As(V)

    As(digested)

    1000

    1500 2000 HCO3

    VFA

    500

    0 0 200 400 600 800

    time (days)

    12 S1. Setting the bar

    GFH Column Leachate

    Equilibrium As Concentration : 25.66ppb

  • 13 S1. Setting the bar

    GFH Column Leachate

    0.00

    100.00

    200.00

    300.00

    400.00

    500.00

    600.00

    0 200 400 600 800

    Time (days)

    Fe

    (in

    pp

    m)

    0

    1000

    2000

    3000

    4000

    As(

    in p

    pb

    )

    Fe (total) As(total)

  • S1. Setting the bar

    Sorb-33 Column Leachate 14

    0 50

    100 150 200 250 300 350 400 450 500 550 600

    0 50 100 150 200 250 300

    Time (days)

    Tot

    al F

    e (m

    g/L

    )

    0 500 1000 1500 2000 2500 3000 3500 4000 4500 5000

    Tot

    al A

    s (p

    pb)

    Total Fe Total As

  • 0

    0.1

    0.2

    0.3

    0.4

    0.5

    0.6

    Frac

    tion

    As

    deso

    rbed

    AA

    GFH

    4.59

    14.96

    12.25

    50.84

    28.21

    152.5

    7 8 9pH

    15 S2. New Protocol Development

    pH Effects

    10

  • 16 S2. New Protocol Development

    Anion’s Effects

    Anion Landfill Leachate Range (in mg/L) (Bagchi, 1994)

    Concentration Used in

    Competition Trials

    (in mg/L)

    Fraction As expected to leach due to

    concentration of anion in LL

    Fraction of total leaching attributable to each anion in the

    SLL-theo

    Activated Alumina Phosphate 0.11- 234 20 0.002 0.04

    Bicarbonate 34- 15,050 1,200 0.008 0.15 Sulfate 105- 4,900 500 0.002 0.04 Silicate 5.1-51 10 0.001 0.02 NOM 76-40,000 200 0.04 0.75

    Granular Ferric Hydroxide Phosphate 0.11- 234 20 0.0007 0.03

    Bicarbonate 34- 15,050 1,200 0.012 0.48 Sulfate 105- 4,900 500 0.0008 0.03 Silicate 5.1-51 10 0.0013 0.05 NOM 76-40,000 200 0.01 0.4

  • TCLP LL WET SL1 SL2 0

    0.2

    0.4

    0.6

    0.8

    1

    1.2

    Extra

    ctan

    t Ars

    enic

    (m

    g/L

    as A

    s)

    AA, 18hr AA, 48hr

    GFH, 18hr GFH, 48hr

    Initial Loading: AA, 31 ppb; GFH, 22 ppb

    17 S2. New Protocol Development

    Reductant + TOC Effect

  • 18 S3. Treatment & Stabilization Options

    AFH Crystallization

    D7

    0

    100

    200

    300

    D14

    0

    500

    1000

    D24

    0

    500

    1000

    1500

    D0

    0 100 200 300 400

    20 30 40 50 60 70

    D42

    0 200 400 600 800

    1000 1200 1400 1600 1800

  • 19 S3. Treatment & Stabilization Options

    As Release & Crystallization

    0.0

    0.1

    0.2

    0.3

    0.4

    0.5

    0.6

    0.7

    0.8

    0.9

    1.0

    0 300 600 900 1200 AGING TIME(Hrs)

    As(t)

    /As(T

    )

    pH7

    pH8

    pH9

    pH10

    pH11

    pH12

  • 20 Broader Implications

    •Arsenic as an elemental contaminant •no destructive technologies •media and speciation transformations only •surrogate for heavy metals, metalloids, radionuclides

    •Arsenic as a redox-sensitive, oxyanion •inverse pH behavior to metals •microbially mediated fate and transport •typically most mobile in reduced form •surrogate for V, Mo, Se, S, Cl, N, P

    •Arsenic as a ‘natural’ contaminant •primarily non-anthropogenic sources •naturally diffuse but anthropogenically concentrated •surrogate for Rn, U, Se, S, F, Br, V

  • 21

    Batch Adsorption Experiments

  • 22 AA Adsorption Edge

    0

    0.2

    0.4

    0.6

    0.8

    1

    4 6 8 10 12 pH

    C/C

    o

    Co = 0.125mM Co = 0.05mM Co = 0.0125mM Co = 0.005mM Co = 0.00125mM

    • Co - Initial arsenic concentration in solution • C - Equilibrium arsenic concentration in solution

  • GFH Adsorption Edge

    Co = Initial concentration of As in solution (total As in the system) C = Concentration of As in solution at equilibrium Solid Loading = 25g/L

    23

    0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9

    5 6 7 8 9 10 11

    pH

    C/C

    o

    Co= 1.66mM Co= 8.33mM Co= 16.6mM Co= 83.3mM

  • 24

    Comparative Leaching Tests

  • 25

  • 26

  • 27 Activated Alumina

    0 100 200 300 400 500 600 700 800 900

    1000

    TCLP WET LL SL1 SL2

    Leac

    hate

    As

    Conc

    . (pp

    b as

    As) 18hr

    48hr

    Concentration of As in solution at equilibrium prior to leaching tests = 21.8ppb Sorbed concentration of As = 1.27mgAs/gAA. Test conditions: No N2 headspace, end-over-end tumbler.

  • 28 Granular Ferric Hydroxide

    0

    200

    400

    600

    800

    1000

    1200

    TCLP WET LL SL1 SL2

    Leac

    hate

    As

    Con

    c. (p

    pb a

    s A

    s)

    18hr

    48hr

    Concentration of As in solution at equilibrium prior to

    leaching tests = 31ppb Sorbed concentration of As = 7.2mgAs/gGFH. Test conditions: No N2 headspace, end-over-end tumbler.

  • 29 Ferric Hydroxide Sludge

    1

    10

    100

    1000

    10000

    100000

    1000000

    10000000

    TCLP WET LL

    Leac

    hate

    As

    Con

    c. (p

    pb a

    s A

    s) 18hr 48hr

    Concentration of As in solution at equilibrium prior to

    leaching tests = 1040ppb Sorbed concentration of As = 20.3mgAs/gFe. Test conditions: No N2 headspace, end-over-end tumbler.

  • 30

    Competitive Anion Effects

  • 31 Activated Alumina Anion Effect Anion (Moles As

    released/ mole

    (Moles As released/

    mole

    (Moles As released/

    mole

    Fraction sorbed As expected to leach due to concentration of anion in LL

    pH7anion pH9)high pH7anio pH9n)low pH7anion)a pH9verage

    Phosphate 279 113 3.05 1.52 9.24 4.69 0.002

    Bicarbonate 0.92 0.58 0.014 0.007 0.043 0.025 0.008

    Sulfate 0.352 0.143 0.017 0.014 0.045 0.028 0.002

    Silicate 12 8.6 0.56 0.68 2.6 2 0.001

    NOM 391 336 0.41 0.23 2.35 1.13 0.04

  • 32 GFH Anion Effect Anion (Moles As

    released/ mole

    (Moles As released/

    mole

    (Moles As released/

    mole

    Fraction sorbed As expected to leach due to concentration of anion in LL

    pH7anion pH9)high pH7anio pH9n)low pH7anion)e

    pH9averag

    Phosphate 357 244 4.02 2.09 10.5 6.07 0.0007

    Bicarbonat e

    8 4 0.027 0.023 0.24 0.11 0.012

    Sulfate 0.698 0.458 0.021 0.005 0.098 0.054 0.0008

    Silicate 32 21 2.1 0.62 5.4 3.7 0.0013

    NOM 1064 374 0.7 0.19 3.9 0.97 0.01

  • 33

    Column Experiment Methods

  • 34 Column Packing Composition Specifications Activated

    Alumina GFH E-33

    Mass of Residual

    1017g 527g 509g

    Total Amount of As

    1.29g 2.86g 2.61g

    Initial Sorbed As Conc.

    1.27mgAs/gAA 5.42mgAs/gGF H

    5.13mgAs/gE33

    Initial equilibrium As

    conc.

    193ppb 25.6ppb 11ppb

    Duration of run 302 days 808 days 274 days

  • 35

    Activated Alumina Column

  • 36 pH

    6

    6.5

    7

    7.5

    0 50 100 150 200 250 300 350

    time (days)

    pH

  • 37 Alkalinity

    0 1000 2000 3000 4000 5000 6000

    0 50 100 150 200 250 300 350

    time (days)

    alk

    alin

    ity

    (m

    g/L

    )

  • 38 ORP

    -25

    -15

    -5

    5

    15

    25

    0 50 100 150 200 250 300 350

    time (days)

    OR

    P (

    mV

    )

  • 39 DOC

    0

    1

    2

    3

    4

    5

    6

    7

    0 50 100 150 200 250 300 350

    time (days)

    DOC

    (g/L

    )

  • 40 Arsenic

    0

    500

    1000

    1500

    2000

    0 40 80 120 160 200 240 280 320

    Time(days)

    Co

    nc

    (pp

    b)

    As(III) As(V)

    As(dissolvedl) As (total)

    * Small amounts of MMA(V), DMA(V) and MMA(III) were also observed in the effluent.

  • 41 Fractional Arsenic Leached

    0

    0.02

    0.04

    0.06

    0.08

    0.1

    0.12

    0 50 100 150 200 250 300 350

    Time (days)

    Fra

    ctio

    nal

    As

    Lea

    ched

  • 42

    GFH Column Results

  • 43 pH

    6

    6.5

    7

    7.5

    8

    8.5

    9

    9.5

    10

    0 200 400 600 800 1000

    days

    pH

  • 44 Alkalinity

    0

    500

    1000

    1500

    2000

    2500

    3000

    3500

    0 200 400 600 800

    days

    Alk

    alin

    ity (m

    g/L)

  • 45 ORP

    -250

    -200

    -150

    -100

    -50

    0 0 100 200 300 400 500 600 700 800

    days

    OR

    P (

    mV

    )

  • 46 DOC

    0

    500

    1000

    1500

    2000

    2500

    3000

    0 100 200 300 400 500 600 700

    days

    DO

    C (m

    g/L)

  • As

    (pp

    b)

    4000 As(III) 3500 As(V) 3000 As(dissolved) 2500 As(digested) 2000

    1500

    1000

    500

    0 0 200 400 600 800

    time (days)

    47 GFH Column Results

  • Fe (m

    g/L)

    600

    400

    500 Fe (dissolved) Fe (digested)

    300

    200

    100

    0 0 200 400

    time (days)

    600 800

    48 GFH Column Results

  • 49 Overall Picture

    0.00

    100.00

    200.00

    300.00

    400.00

    500.00

    600.00

    0 200 400 600 800 1000

    Time (days)

    Fe

    (in

    pp

    m)

    0

    1000

    2000

    3000

    4000

    As(

    in p

    pb

    )

    Fe (total) As(total)

  • 50 Fractional Arsenic Leached

    0 0.05 0.1

    0.15 0.2

    0.25 0.3

    0.35 0.4

    0.45 0.5

    0 200 400 600 800 1000

    time (days)

    Fra

    ctio

    nal

    As

    Lea

    ched

  • Fe(

    mg

    /L)

    250

    200

    150

    100

    50

    0 0 200

    >5U 0.8U

  • As

    (p

    pb

    )

    2500

    2000

    1500

    1000

    500

    0

    >5U 0.8U

  • 53

    E-33 Column Results

  • 54 pH

    6

    7

    8

    0 50 100 150 200 250 300

    time

    pH

  • 55 Alkalinity

    900

    1400

    1900

    2400

    0 50 100 150 200 250 300

    time

    Alk

    alin

    ity

    (m

    g/L

    )

  • 56 E-33 Column Results

    0

    20

    40

    60

    80

    0 50 100 150 200 250 300

    time (days)

    Fe

    (mg

    /L)

    Fe(II) Fe(III) Fe(dissolved) Fe(total)

  • 57 E-33 Column Results

    0 1000 2000 3000 4000 5000

    0 50 100 150 200 250 300

    time (days)

    As

    (PP

    B)

    As(III) As(V) As(dissolvedl) As(total)

  • 58 Fractional Arsenic Leached

    0

    0.05

    0.1

    0.15

    0.2

    0.25

    0.3

    0 50 100 150 200 250 300

    Time (days)

    Fra

    ctio

    nal

    As

    Lea

    ched

  • 59

    Iron Sludge Column Results

  • 60 pH

    6

    6.5

    7

    7.5

    8

    8.5

    9

    0 20 40 60 80 100 120 140 160

    Time (days)

    pH

  • 61 Alkalinity

    3000

    4000

    5000

    6000

    7000

    8000

    0 20 40 60 80 100 120 140 160

    Time (days)

    Alk

    alin

    ity

    (mg

    /L)

  • 62 ORP

    -400

    -300

    -200

    -100

    0

    100

    200

    300

    0 20 40 60 80 100 120 1

    Time (days)

    OR

    P (

    mV

    )

    40

  • 63 Arsenic

    0

    50000

    100000

    150000

    200000

    250000

    0 20 40 60 80 100 120 140

    Time (days)

    As

    (pp

    b)

    As (total) As (dissolved) As(III) As(V)

  • 64 Iron

    0.00 100.00

    200.00 300.00 400.00

    500.00 600.00

    700.00 800.00

    0 20 40 60 80 100 120 140

    Time (days)

    Fe

    (in

    mg

    /L)

    Fe (total) Fe (dissolved) Fe(II) Fe(III)

    Assessment and Disposal of Arsenic Treatment ResidualsPhilosophy and FormatChanges and ImpactsTest/Landfill CharacteristicsOur Corollary ResearchSolid Media LeachingResiduals Assessment TestsS1. Setting the barLandfill Simulation ColumnsS1. Setting the barGFH Column LeachateS1. Setting the barSorb-33 Column LeachateS2. New Protocol DevelopmentpH EffectsS2. New Protocol DevelopmentAnion’s EffectsS2. New Protocol DevelopmentReductant + TOC EffectS3. Treatment & Stabilization OptionsAFH CrystallizationS3. Treatment & Stabilization OptionsAs Release & Crystallization


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