biological struvite crystal formation in sludge …...options for p recovery primary sed. second....

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Dr Ana Soares, Lecturer Biological Engineering Copyrighted Biological struvite crystal formation in sludge dewatering liquors

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  • Dr Ana Soares, Lecturer Biological Engineering Copyrighted

    Biological struvite crystal formation in sludge dewatering liquors

  • Phosphorus: a pollutant or a resource?

    Guideline

    UWTD

    (91/271/EEC)

    2 mg/L (10k-100k p.e.)

    1 mg/L (>100k p.e.)

    New targets 0.01-0.1 mg/L P

    Rock Phosphate Monthly Price -

    US Dollars per Metric Ton

    http://www.indexmundi.com/commodities

  • World P resources

    Gilbert N: The disappearing nutrient. Nature 2009 461: 16–718

    Stopped exporting in 1997

    Planned bans

    on exportation

    In gigatonnes

  • Recovery of phosphorus from wastewater enough?

    Municipal

    wastewater

    treatment

    pant P

  • Options for P recovery

    Primary sed. Second. sed. Tertiary treatment

    Treated

    effluent

    Sludge

    Sludge

    Large

    items

    Grit

    Screens Grit

    chamber

    Activated sludge

    or trickling filter

    Sludge

    Biogas Anaerobic digester

  • P recovery from sludge liquors

    Struvite chemical precipitation

    + Well known process installed at full-scale with a market

    +/- Recovery of 90% of phosphorus (10% left in the wastewater)

    - Needs high phosphorus streams >100 mg/L

    - Crystallisation through chemical process with chemical addition

    Le Corre KS, Valsami-Jones EB, Hobbs PC, Parsons SA: Phosphorus recovery from wastewater by struvite crystallization: A review. Crit Rev

    Environ Sci Technol 2009, 39: 433–477.

    Pratt C, Parsons SA, Soares A, Martin BD: Biologically and Chemically Mediated Adsorption and Precipitation of Phosphorus from Wastewater.

    Trends in Biotechnology

  • Sludge liquors have high P – other ways to recover P?

    Sustainable

    (no chemicals)

    Versatile

    (range of [P] )

    High quality effluent

    Usable for wastewater

    mixed matrix

    High yield, good product

    quality

  • Investigate the suitability of selected bacteria to produce struvite in wastewater and dewatering liquors

    Bio-mineralization: biological formation of inorganic materials

    Over 60 different minerals have been identified, including struvite and CaP

    Widespread property in environment/nature

    Well studied in biomedical sciences (e.g.: kidney stones)

  • Bio-mineralization: Known mechanisms

    Nucleus Crystal Vacuole Nucleus Crystal Vacuole

    Nucleus

    Crystal

    Extracellular microenvironment

    Crystal

    Intracellular crystal production

    Extracellular crystal production

    Bacteria

    Bacteria

  • Bio-mineralization bacteria selection: Literature information

    Myxococcus xanthus: soil bacteria, EXTRACELLULAR crystal production observed after 2 days in synthetic media

    Bacillus pumilus: soil bacteria, EXTRACELLULAR crystal production observed after 6-20 days in synthetic media

    Halobacterium salinarum: Aquatic halophilic bacteria, INTRACELLULAR crystal production observed after 3-4 days in synthetic media

    Brevibacterium antiquum: permafrost soil bacteria, INTRACELLULAR crystal production observed after 2-3 days in synthetic media

  • Bio-mineralization bacteria selection: Cultivation in synthetic media

    Strains Growth rate

    (1/h)

    Dry weight

    (mg/L)

    Myxococcus xanthus 0.013 2160

    Bacillus pumilus 0.039 720

    Halobacterium salinarium 0.042 63

    Brevibacterium antiquum 0.027 980

    Negative control: media without bacteria – no crystal

    production

  • Bio-mineralization bacteria selection: Cultivation in wastewater

    Primary sed. Second. sed.

    Treated

    effluent

    Sludge

    Sludge

    Large

    items

    Grit

    Screens Grit

    chamber

    Activated sludge

    Sludge

    Biogas Anaerobic digester Sludge liquors:

    PO4-P: 30 mg/L

    NH4-N: 629 mg/L

    Mg: 39 mg/L

    WW

    PO4-P: 2.3 mg/L

    NH4-N: 70 mg/L

    Mg: 17.8 mg/L

    Full-scale wastewater treatment plant (UK)

    PE 570,000.

    Thick./dewatering

  • Bio-mineralization bacteria selection: Cultivation in wastewater

    Typical µmax:

    Denitrifiers= 0.1 1/h; Methanogens= 0.02 - 0.002 1/h;

    Anammox = 0.001 - 0.004 1/h

    Wastewater M.

    xanthus

    B.

    pumilus

    H.

    salinarium

    B.

    antiquum

    Settled

    wastewater

    Growth rate

    (1/h)

    Negligible 0.001 Negligible

    0.004

    Crystal dry

    weight

    (mg/L)

    - 137 - 113

    Sludge

    dewatering

    centrifuge

    liquors

    Growth rate

    (1/h)

    Negligible

    0.001 0.002 0.002

    Crystal dry

    weight

    (mg/L)

    - 213 - 226

    Negative control: Wastewater not inoculated – no crystal production

  • Crystal characterisation

    Crystals formed by B.antiquum in centrifuge sludge liquor were

    approximately 250 µm

  • Crystal characterisation

    SEM images in sludge dewatering

    centrifuge liquors

    struvite

    struvite

    Scanning electron microscope with energy

    dispersive x-ray spectroscopy (SEM-EDX)

  • Effluent quality

    Sludge dewatering centrifuge liquors

    Settled wastewater

    PO4-P

    (mg/L)

    NH4-N

    (mg/L)

    Mg

    (mg/L)

    PO4-P

    (mg/L)

    NH4-N

    (mg/L)

    Mg

    (mg/L)

    Initial concentration

    30.5 629.0 38.9 Initial concentration

    7.5 70.0 22.6

    After cultivation

    with B.

    pimulus

    2.1 122.5 18.7 After cultivation

    with B.

    pimulus

    2.0 30.0 9.0

    After

    cultivation

    with B. antiquum

    1.5 117.5 21.4 After

    cultivation

    with B. antiquum

    2.1 31.0 9.5

    B. pimulus

    removal

    93% 81% 52% B. pimulus

    removal

    73% 57% 60%

    B. antiquum

    removal

    95% 81% 45% B. antiquum

    removal

    72% 56% 58%

  • Bio-struvite vs. chemical struvite (10,000 m3/day wastewater treatment plant producing 500 m3/day of sludge liquors)

    * Costs used in chemical precipitation are from 2001 (Jaffer et al.,); struvite price $1500/ton

    http://biomassmagazine.com/articles/1838/from-problem-to-profit

    Parameter Biological struvite Chemical struvite

    Production Kg/day 120 100

    Capital costs

    £ Fermentation

    reactor (10 days HRT)

    630,000 Precipitation

    reactor

    425,000

    Blowers and

    diffusers

    Not

    known

    Blowers and

    diffusers

    825,000

    Filtration unit 100,000 Desludge pump 75,000

    Total capital

    costs

    £ total 730,000 total

    1,325,000

    Operating costs £/year Electricity

    10,000

    Electricity 3,500

    Chemical costs 13,000

    Total operating

    costs

    £/year total

    10,000

    total

    16,500

    Post treatment Likely not to be required Needs recirculation to the head of

    the works

    Income = £40,734

    Total Opex = £10,000

    Income = £33,945

    Total Opex = £16,500

    http://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profithttp://biomassmagazine.com/articles/1838/from-problem-to-profit

  • Bio-struvite producing bacteria can be the “anammox” for phosphorus?

    Microbial characterization

    (μ, Ks, temp, nutrients, pH,

    etc.)

    Reactor

    design

    Struvite separation

  • Conclusions

    Bacteria can produce struvite crystals in wastewater in simple way (no optimisation yet!)

    Microscope analysis showed presence of crystals as early as 3 days and visible crystals were seen in cultures after 10 days reaching up to 250 µm.

    Crystals can be separated by filtration/centrifugation

    The final concentration of phosphate in sludge centrifuge liquors reached 1.5 mg/L, indicating a 95% P and 55-86% ammonia removal

    The process can potentially be economically attractive

  • New flowsheets for wastewater treatment

    Screen

    Primary

    Sedimentation

    Raw

    wastewater

    anMBR

    1 ry

    / 2 ry

    sludge

    Thickener

    Sludge supernatant ( Return liquor )

    Stabilised sludge to land

    Anaerobic digester

    Sludge recirculation

    loop to heat exchanger

    Gas

    engine

    Imported grid

    electricity Digested sludge pump

    Primary

    sludge

    pump

    Thickened

    Primary

    sludge

    pump

    Disposal of gross

    solids

    Produced biogas

    Treated

    effluent

    Nutrient rich

    eluent

    N - C

    o n

    t a c t o

    r

    P - C

    o n

    t a c

    t o r

  • Phosphorus removal media

    HCO3-

    SO42-

    SO42-

    SO42-

    HCO3-

    HCO3-

    NO3-

    Cl-

    Cl-

    Cl-

    Cl-

    Cl- PO43-

    PO43-

    PO43-

    PO43- PO4

    3-

    PO43-

    PO43-

    Capacity 2 g P/ kg media

    Regeneration 5% NaOH

  • Compare technologies R

    eso

    urc

    e r

    eco

    ve

    ry p

    ote

    nti

    al

    Sludge to land Chemical

    struvite Adsorption

    processes

    Phosphorus recovery technology

    Bio-struvite

  • Thank you for your attention

    [email protected]

    www.cranfield.ac.uk/SAS

    Thank you to: Yorkshire Water and Severn Trent

    Further reading:

    Soares A, Veesam M, Simoes F, Wood E, Parsons SA, Stephenson T. 2013. Bio-struvite: A new route to recover phosphorus from wastewater. CLEAN - Soil, Air, Water. In Press.

    mailto:[email protected]://www.cranfield.ac.uk/SAS