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 CSIRO MATERIALS SCIENCE AND ENGINEERING Ammonia stripping for N recovery Tim Muster | Group Leader: Functional Interfaces & Coatings 1 st May 2012
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Tim Muster - Ammonia Stripping for N Recovery

Oct 07, 2015

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Ammonia Stripping
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  • CSIRO MATERIALS SCIENCE AND ENGINEERING

    Ammonia stripping for N recovery

    Tim Muster | Group Leader: Functional Interfaces & Coatings

    1st May 2012

  • Nitrogen

    [CO2] = 387Boundary = 350

    Ammonia Stripping for N Recovery

    J. Foley, Scientific American, April 2010, pp 38 -44

    N = 133 Mt/yrBoundary = 39

    P = 10 Mt/yrBoundary = 12

    Extinction rate > 100 species/MyrBoundary = 10

  • IS AMMONIA in wastewater a WASTE or RESOURCE?

    Global ammonia production ~177m tonnes (2008)

    Energy intensive to make; 40 GJ/tonne or 10.2 MWh/t

    Nitrogen is initially present as NH3 in wastewater (urea + protein breakdown)

    At ~40-45 mg/l, accounts for >55% of total N of treatment plant influent

    Builds up to high concentration during anaerobic digestion

    Nitrogen & Ammonia Summary

    Builds up to high concentration during anaerobic digestion

    Limits methane production

    Encourages struvite precipitation

    Special properties

    Ammonia is highly water soluble

    Present as ammonium ion below pH 9 (pKa = 9.5).

    Ammonia Stripping for N Recovery

  • Biological

    - Nitrification/denitrification

    - Many variations: SBR, Bardenpho, Anammox etc.

    Physico-chemical

    - Ion exchange

    Methods for N Removal

    Generally cost effectiveCan be energy-intensive due to aeration/mixing/carbon additionsProduction of N2O (strong GHG)

    - Ion exchange

    - Breakpoint chlorination

    - Stripping

    - Electrodialysis

    - Reverse Osmosis

    - Precipitation

    Ammonia Stripping for N Recovery

    Table: Comparison of removal costs for ammonia-N

    Process Cost $/kg N removed or captured Captured ammonia

    Nitrification/Denitrification 1.8* No

    CASTion ammonia recovery 6.7* Yes

    Air stripping 2.4* Yes

    Clinoptilolite (adsorption/exchange) 2.8* Yes

    Commercial return for ammonia 0.4

    Data: *Phillips et al. (2011)

  • Ammonia Stripping Many ConfigurationsEncouraged by:

    Increase air : water contact

    Increased Temperature

    High pHW

    a

    t

    e

    r

    i

    n

    Ammonia Stripping for N Recovery

    Aerated Column

    Packed Column

    Spray(or vacuum) Lagoon

    A

    i

    r

    i

    n

    Air flow over lagoon

  • Reduction of ammonia to nitrogen gas:

    - Can be achieved by chemical addition or electrochemical oxidation

    Chloride oxidation

    Ammonia Stripping for N Recovery

    During electrochemical oxidation of chloride, chloride ion is replenished.

  • Precipitation with Phosphorus as Struvite

    Many processes: Phostrip, Prisa, DHV Crystalactor, Ostara, Prophos,

    Multiform Harvest, Recyphos, Phosiedi, Berlin, Airprex,

    Fixphos

    Wastewater Primary Treatment

    SludgeReturn30 ppm P1000 ppm NH

    Ammonia Stripping for N Recovery

    P / (N)Fertilizer

    Mg2+, Ca2+caustic delivery,

    or addition of adsorbent

    Fermentation

    Sludge

    Anaerobic Digestion

    CentrifugeCentrate600 ppm P1200 ppm NH3

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    1000 ppm NH3

    Nitrogen is still in excessadditional technology required to meet N requirements

  • Overall: Capture the value of Water + C + N + P

    Likely return value: Water > Carbon > Phosphorus > Nitrogen

    Likely cost of removal: Carbon > Nitrogen > Phosphorus

    What to do with nitrogen:

    Approach

    What to do with nitrogen:

    -reduce cost of removing nitrogen (with capture of ammonia if possible)

    -WWTP influent starts off as ammonia

    aim to develop method for physical separation of NH3 into both vapour and solid phase

    - Developing a combined process:

    Ammonia Stripping for N Recovery

    Stripping Breakpoint chlorination Precipitation

  • Wastewater treatment will continue to transform into Energy and Resource Recovery Centres

    Need to develop concentration and separation processes

    There is an opportunity to combine several physico-chemical methods to improve ammonia-N removal and recovery

    Summary

    There is an opportunity to combine several physico-chemical methods to improve ammonia-N removal and recovery WATCH THIS SPACE

    Question: what are the industry priorities for these processes?

    Now: Sanitation > Water > N > Heavy Metals > C > P?

    The future: Sanitation > Water > C > P > Heavy Metals > N?

    Ammonia Stripping for N Recovery

  • Thank youThank youTim MusterGroup Leader: Functional Interfaces & Coatings

    t +61 3 9545 7964e [email protected] www.csiro.au/

    CSIRO MATERIALS SCIENCE AND ENGINEERING