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TRANSCRIPT
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Denitrifying Bioreactors: Opportunities and Challenges for Managing
Offsite Nitrogen Losses
A. J. Gold1, L. A. Schipper2 and K. Addy1
1University of Rhode Island, USA 2University of Waikato, NZ
FAO/IAEA Int’l Symposium on Managing Soils for Food Security and Climate Change Adaptation and Mitigation
Vienna, Austria July 24, 2012
IAEA-CN-191-42
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Fish Kill, Rhode
Island, USA
Excess nitrogen from agriculture:
• Stimulates algal growth; fishkills; degrades coastal habitats
• Generates a potent greenhouse gas, nitrous oxide (N2O = 300 CO2 equivalents)
• Drinking water contaminant
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Offsite nitrate losses can be removed within natural denitrification sinks
NO3- NO2- NO N2O N2 • Electron donor (labile carbon) • Anaerobic conditions • Extended retention times • Appropriate temperatures
Nitrate
Organic soils, Riparian forest buffer
Nitrogen gas
from denitrification
Schipper, U. of Waikato
Shallow groundwater flow
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Filling trench box with wood chips
Photo courtesy of Betty Buckley, URI Graduate School of Oceanography
Where natural sinks are missing, denitrifying bioreactors can treat nitrate-laden waters:
© THE UNIVERSITY OF WAIKATO • TE WHARE WANANGA O WAIKATO, Schipper et al.
• Requires nitrification in advance of bioreactor • High nitrate removal rates if designed properly • Labile C sources induce anaerobic conditions • Micro-organisms appear to be self-seeding
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Denitrifying Walls: Rely on intercepting natural groundwater flow
Gold and Addy, 2008
• In deep aquifers, substantial nitrate can bypass wall bioreactor
Schipper et al., 2010
• Work well close to source
• Work well in shallow aquifers
15 m
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Denitrification beds: Intercept nitrate from concentrated flows
Schipper, et al. 2010. Ecol. Engin.
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Wood chip denitrifying bed placed into channel
(Robertson et al. 2009)
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Denitrifying bioreactors: Factors controlling nitrate removal rates and denitrification
• N source : Nitrification must precede bioreactor
• Retention time: Variations in flow rate must be considered (minimum recommended > 0.25 days)
• Temperature (rates increase with high temperatures)
• Carbon source: Lability; longevity; porosity
Year
96 97 98 99 00 01 02 03 04 05
Nitr
ate (
mg N
L-1 )
0
2
4
6
8
10
12
Upslope
Downslope
Schipper and Vojvodic-Vukovic (2001)
10 years performance of denitrification wall
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Nitrate removal rates with different carbon sources
Pinus
radiata
(mea
n)
Har
dwoo
d
Whe
at stra
w
Gre
en w
aste
Maize
cob
s 0
2
4
6
8
10
12
14
16
18
20
Nitra
te r
em
oval ra
te (
g N
m-3 d
-1) 24
oC
14oC
Note that temperature generally increases removal rates
Lability
Longevity
Wood chips
Cameron and Schipper, 2010
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Wood chip longevity: Little decline in rates over
15 years of observation
Temperature (oC)
Ra
te (
mg
N L
-1 d
-1)
Comparison of Year 1-15 Removal Rates
0 5 10 15 20 250
4
8
12
Year 1 columns (sawdust)Year 15 column (sawdust)Year 1-7 field PRBy = 0.17 exp(0.16x), R2 = 0.96
Robertson, 2010.
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15N studies to determine mechanism of NO3-
removal: Natural abundance
Length (m)
0 40 80 120 160 200
15
N
-15
-10
-5
0
5
10
15
20
25
15N-N2 headspace equilibrium
15N-N2 vacuum extraction
15N-NO3
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Note increasing enrichment of nitrate along length of bed
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Push-Pull Method: In situ denitrification capacity through 15NO3
- enrichment
Push Pull
Water Table
Introduced
plume
2 cm
mini-piezometer
• Pump groundwater • Amend with 15NO3
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• Push (inject) into well • Incubate • Pull (pump) from well • Analyze samples for
15N2 and 15N2O
(products of microbial denitrification)
Addy et al. 2002, JEQ
15NO3-
15N2, 15N2O
Wood Chips
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Push pull A
Push pull B
N2 conc. along
In vitro DR
Measured nitrate
Denitrification r
ate
(g N
m-3
d-1
)
0
10
20
30
40
50
the bed
(C2 H
2 inh.)
removal rate
Push-Pull 15N method shows denitrification is the main mechanism for nitrate removal (Acetylene-block
overestimated rates)
Warneke, et al. 2011
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Adverse effects?
• Can generate greenhouse gases N2O, CH4, CO2 • Dissolved carbon leaving bed – problem at
start up
• H2S – possible health hazard
• Methyl mercury
Managing adverse effects: Requires balancing NO3
- load with retention time
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Denitrifying Bioreactor: Nitrous oxide emission
0
1
2
3
4
5
6
7
April June Sept Nov Jan
N2O
flu
x in u
mol m
-2
min
-1
On average < 0.9 % of NO3--N removed emitted as N2O gas emissions
(IPCC: Groundwater N2O gas emissions as high as 1.5% of NO3—N leached)
Warneke et al., 2011. Ecol. Engin.
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Future Directions and Challenges
Woodchip/wetland bed, H. Leverenz, UC Davis
Opportunities to combine carbon bioreactors with
wetlands for food or fiber
Acknowledgements: This material is based upon work supported by the National Institute of Food and Agriculture, U.S. Department of Agriculture, under Agreement No. 2011-51130-31120. Contribution from Joint FAO/IAEA CRP: “Strategic placement and area-wide evaluation of water conservation zones in agricultural catchments for biomass production, water quality and food security”
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Selected References
Addy, K, D.Q. Kellogg, A.J. Gold, P.M. Groffman, G. Ferendo and C. Sawyer. 2002. In situ push-pull method to determine ground water denitrification in riparian zones. J. Environ. Qual. 31:1017-1024.
Cameron S.G. and Schipper, L.A. 2010. Nitrate removal and hydraulic performance of carbon substrates for potential use in denitrification beds. Ecol. Engin. 36 : 1588-1595.
Robertson, W.D. 2010. Nitrate removal rates in woodchip media of varying age. Ecol. Engin. 36: 1581-1587.
Robertson, W.D. and L.C. Merkley. . 2009. In-Stream Bioreactor for Agricultural Nitrate Treatment. J. of Environ. Qual. 38:230-237
Schipper, L.A., W.D. Robertson, A.J. Gold, D.B. Jaynes, S.C. Cameron, 2010. Denitrifying bioreactors—An approach for reducing nitrate loads to receiving waters. Ecol. Engin. 36:1532-1543.
Schipper, L.A., M. Vojvodic-Vukovic. 2001. Five years of nitrate removal, denitrification and carbon dynamics in a denitrification wall. Water Research. 35: 3473–3477.
Warneke, S.; Schipper, L.A.; Bruesewitz, D.A.; Baisden, W.T. 2011. A comparison of different approaches for measuring denitrification rates in a nitrate removing bioreactor. Water Research. 45: 4141-4151.