Treatment of Contaminated Water by Constructed Wetlands: an old Technology revisited
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Lecture series Chemicals in the Environment Treatment of Contaminated Water by Constructed Wetlands: an old Technology revisited Hermann J. Heipieper Department of Environmental Biotechnology Helmholtz Centre for Environmental Research – UFZ Leipzig, Germany Leipzig, 16 October 2012
Constructed Wetlands for Sewage and Wastewater treatment Sewage Irrigation Fields Were used in Europe for the treatment of domestic sewage since the end of the 19th century and were substituted by modern waste water treatment plants after the second world war
Renaissance of Constructed Wetlands Parking areas along the German Autobahnen „Hundertwasserhaus“ in Vienna
Comparison of constructed wetlands with other wastewater treatment technologies Trickling Filter Fixed Bed Reactor Activated Sludge Systems Constructed Wetlands
Comparison of investment and running costs of constructed wetlands and 3 other wastewater treatment technologies Costs / PE (€) Investment 4 PE 8 PE 20 PE 50 PE Treatment Plant Size Trickling Filter Fixed Bed Reactor Activated Sludge Systems Constructed Wetlands Running Costs / PE*year (€) 4 PE 8 PE 20 PE 50 PE Treatment Plant Size PE = Population equivalent or unit per capita loading is the number expressing the sum of the pollution load produced during 24 hours by industrial facilities as the pollution load in household sewage produced by one person. One PE unit equals to 54 grams of Biochemical Oxygen Demand (BOD) per 24 hours
Wetlands in nature and for wastewater treatment Sun phytovolatilization Plants volatilization phytoaccumulation ☺☺ contaminants ☺☺ adsorption ☺☺ biodegradation ☺☺ filtration Rhizosphere microorganisms
Constructed Wetlands (CWs): Role of plants Input of organic compounds and O2 into the rhizosphere uptake, assimilation aerobic zone accumulation and metabo- lisation of inorganic ions Micro- rhizodeposition products organisms Role of soil matrix SRB Corg. + SO42- → CO2 + S2- anaerobic zone adsorption, ion exchange S2- + Me2+ → MeS↓ filtration, surface for biofilms Role of microorganisms Sediment degradation/transformation of organic and inorganic compounds In the rhizosphere, density and diversity of microorganisms is 10 to 100-times higher than in the surrounding bulk soil
The rhizospheric effect Aerobic conditions S- + 2 O2 = SO42- rhizospheric effects Anaerobic conditions S- + metals (e.g. FeS) black precipitation
CWs with their macro- and micro-gradients macro- and microgradients Page 11
Mosaic structure of aerobic and anaerobic micro-niches in the root zones Helophytes Electron acceptor Electron donor (oxygen) (rhizodeposition products, root exudates) The actual parameters (rH, oxygen concentration etc.) do not reflect the actual net flow of oxygen and rhizodeposition products! Influencing factors: Plant species Climatic conditions (sun, temperature) Water composition (organics, electron acceptors, pH, buffer capacity) Hydraulic conditions (stagnant or flowing pore water)
Aerenchyma of helophytes e.g. Juncus effusus biologie.tu-dresden.de With the help of these air-filled cavities in their stems, which allows exchange of gases between the shoot and the root, helophytes are able to provide their submerged hypoxic roots with oxygen
Catabolic activity in the rhizosphere Plants provide the rhizosphere with organic compounds such as: alcohols, organic acids, sugars, amino acids Courtesy of Alvaro Gonzalias • supply carbon source • stimulate bacterial degradation Transport of oxygen to the roots allows aerobic degradation Activities only with active photosynthesis
Bioremediation space Nutrients, electron acceptors O2 Micro/macro geography Microorganisms Adapted from: de Lorenzo V., Curr. Opin. Biotechnol. 2008. 19:579-589
Sensors for T, rH, O2 Water jacket T=6 °C Magnetic stirrer Laboratory system for measuring the oxygen input 9
1.6 Max. Oxygen Release Rate [mg h -1 plantlet -1 ] 1.4 TyphaT. latifolia latifolia 1.2 J.effusus Juncus effusus 1 0.8 0.6 0.4 0.2 0 -300 -200 -100 0 100 Eh [mV] Maximum oxygen release rates of individual experiments with several plantlets of T. latifolia and J. effusus depending on the corresponding redox potential (Wießner et al. 2002. Int. J. Phytorem. 4, 1-15)
Oxic-anoxic interfaces and gradients O2-gradients Capillary fringe in soils Root zone of plants Microbial mats
Wastewater Treatment in Constructed Wetlands Advantages Disadvantages • low initial costs • sensitive system • low running costs • high demand on ground • provision of habitats • seasonal fluctuations • construction with local • need of biological research materials
Challenges of Wetland Research at the UFZ Hygienisation (UBZ, UBT) Generation of climate-relevant gases (ANA, BOPHY, HDG, MET) Technology C and S sequestration development (ANA, CATHYD) together with UBZ Removal of recalcitrants of low concentration UBZ - Langenreichenbach – pharmaceuticals … (ANA, UBZ, ECOTOX, GWS) Costs (Root mat filter UBZ - Langenreichenbach technology)
Investigations in the CW Pilot Plants in Leuna and Bitterfeld Zhongbing Chen, Eva Seeger, Mareike Braeckevelt, Shubiao Wu, Oksana Voloshchenko et al.
Types of ponds/constructed wetlands A D B E C A: pond with floating plants B: pond with submersed water plants C: pond with emersed waster plants different intensities D: CW, horizontal subsurface-flow of wastewater to air E: CW, vertical flow and root contact! 3
Constructed Wetlands for treatment contaminated groundwater in Leuna phytovolatilization deep volatilization groundwater unsaturated saturated zone oxic anoxic anoxic O2 groundwater locally flow oxic . mO2 ~ 10 g m-2 d-1
Constructed Wetlands for treatment contaminated groundwater in Leuna Phragmites australis m 5 M. Kästner, 2007 1.1 m SEITE CITE Programmtag 2010
Degradation of Benzene in the Pilot Plant Leuna A1 A6 A2 A3 A5 A1 A2 A4 25,000 20,000 Benzol [µg/l] 15,000 • (A1) horizontal flow planted 10,000 and unplanted soil filters 5,000 • Benzene degradation only 0 occurs in the planted soil 2.5.09 12.5.09 22.5.09 1.6.09 11.6.09 21.6.09 1.7.09 filter Date Outflow unplanted soil filter Outflow planted soil filter Inflow
Mass balance 87.8% benzene 85.7% 88.8% 9.1% 8.1% 11.2% 2.1% 3.1% 3.1% 24.2% 1.0% 43.5% 18.0% 56.5% 37.3% MTBE 32.3% 38.5% 5.0% Plant root mat 38.5% 6.2% worst-case scenario best-case scenario data-based scenario Microbial degradation } Surface volatilization Phytovolatilization Accumulation, Plant uptake Phytodegradation Seeger et al. 2011, EST 45, 8467-8474
Mass balance 87.8% benzene 85.7% 88.8% 9.1% 8.1% 11.2% 2.1% 3.1% 3.1% 1.0% 24.2% 43.5% 18.0% 56.5% 37.3% MTBE 32.3% 38.5% 5.0% 38.5% 6.2% Plant root mat worst-case scenario best-case scenario data-based scenario Microbial degradation } Surface volatilization Phytovolatilization Seeger et al. 2011, Accumulation, Plant uptake EST 45, 8467-8474 Phytodegradation
Mass balance 87.8% benzene 85.7% 88.8% 9.1% 8.1% 11.2% 2.1% 3.1% 3.1% 1.0% 24.2% 43.5% 18.0% 56.5% 37.3% MTBE 32.3% 38.5% 5.0% 38.5% 6.2% Plant root mat worst-case scenario best-case scenario data-based scenario - very low emissions of biodegradable volatile compounds (benzene) Microbial degradation - high emissions of hardly degradable compounds (MTBE) } Surface volatilization Phytovolatilization Seeger et al. 2011, Accumulation, Plant uptake EST 45, 8467-8474 Phytodegradation
Nitrogen transformation processes CWs have favorable conditions for partial nitrification and anammox Canfield et al. 2010. Science. 330:192-196
Investigations in the CW Pilot Plant in Langereichenbach Otoniel Carranza, Monika Möder, Jaime Nivala, Luciana Schultze-Nobre et al.
UBZ ecotechnology research facility “Langenreichenbach” Modified from Headley et al. (2011) Test TEST TES11
Selected substances Substance Use Log inlet Structures Kow (µg L-1) Galaxolide Personal care product 5.7 4.27 ± 4.42 Tonalide Personal care product 5.7 0.48 ± 0.47 Triclosan Personal care product 4.76 1.59 ± 0.46 Carbamazepi Pharmaceutical 2.45 11.85 ± 12.06 ne Caffeine Pharmaceutical 0.16 31.77 ± 30.02 Ibuprofen Pharmaceutical 3.97 30.96 ± 10.13 Diclofenac Pharmaceutical 4.5 9.55 ± 3.47 Naproxen Pharmaceutical 3.18 3.17 ± 0.87 Ketoprofen Pharmaceutical 3.12 4.90 ± 1.06 Techn. Phenolic estrogenic disruptor 4.5 5.52 ± 2.47 Nonylphenol chemical Bisphenol A Phenolic estrogenic disruptor 3.64 Test TEST 6.63 ± 7.11 chemical TES Carranza, O. et al. 2012
Sampling approach 75.0 % 50.0 % 25.0 % 12.5 % 12.5 cm 50.0 cm Modified from Hijosa-Valsero et al. (2010) Test TEST TES
Analytical procedure SPE Multicomponent GC-MS for the quantification of pharmaceuticals 1. Filtration Neutral 2. pH conditioning Galaxolide Tonalide 3. Extract sample Caffeine through cartridge Carbamazepine 4. Drying cartridges + derivatization Ibuprofen 5. Elution with Methanol Naproxen Triclosan Bisphenol A Ketoprofen 6. Evaporation to 1 mL Diclofenac Techn. Nonylphenol 7. Cleanup if needed Test TEST Carranza, O.TES et al.132012
Overall removal efficiencies 0.16 3.12 3.18 3.97 4.5 5.7 2.45 4.5 4.76 3.64 5.7 Test O.TEST Carranza, et al. 2012 TES
POF III: Controlling Chemicals’ Fate
Investigations in the Planted Fixed Bed Reactors PFR Zhongbing Chen, Arndt Wiessner, Uwe Kappelmeyer, Paula Martinez, Luciana Schultze- Nobre, Vianey Marín Cevada et al.
UFZ - Phytotechnicum
Linking water and soil research: Multiphasic process analysis in Planted Fixed- Bed Reactors (PFR)
Experimental tools: Macro-gradient free test system for simulating root-near processes e.g.: - Routes and interrelations of C, N and S transformations - Sulphur immobilization stability - Toxicity effects - Toluene degradation (Planted Fixed Bed Reactor - PFR) (Kappelmeyer, U. et al. 2002)
Planted Fixed Bed Reactors PFR
Planted Fixed Bed Reactor with Juncus effusus 200 150 Oxygen (µg/L) / Redox Potential (mV) 100 50 0 04.07.05 05.07.05 06.07.05 07.07.05 08.07.05 09.07.05 10.07.05 11.07.05 12.07.05 -50 -100 -150 -200 Diurnal oscillation of O2 availability -250 Redox [mV] Oxygen [µg /L] Wießner et al. 2005. Water Res. 39:248-256.
Is the catabolic activity of bacteria changing according to oxygen and redox fluctuations? z z z z z z z zz z zz Courtesy of Dr. Marcell Nikolausz
PFR 5 and 6 planted with Juncus effusus PFR 6 PFR 5 Benzoate + Toluene
Toluene concetration (mg/L) 27 .A 0 5 10 15 20 25 30 35 pr . 2. M ai . R6 In R5 In 7. M ai . 12 .M R6 Out R5 Out ai . 17 .M ai . 22 .M ai . 27 .M Date ai . 1. Ju n. 6. Ju n. 11 .J un . 16 .J un . PFR 5 and 6 planted with Juncus effusus
PFR 5 Deltaproteobacteria "Bacteroidia" "Planctomycetacia" Illumina sequences Holophagae 16S rRNA gene (V5-V6) Chloroplast Subdivision3 Chlamydiae "Sphingobacteria" Clostridia Proteobacteria (70-80%) Actinobacteria Alphaproteobacteria • Most abundant phylum: Gammaproteobacteria Betaproteobacteria • Some diversity differences between the two PFRs PFR 6 Deltaproteobacteria "Bacteroidia" "Planctomycetacia" Holophagae Chloroplast Subdivision3 Chlamydiae "Sphingobacteria" Clostridia Actinobacteria Alphaproteobacteria Gammaproteobacteria Betaproteobacteria
Possible Target enzymes in PFR TOL (Xylene monooxygenase) Baldwin et al.2003 TOD (Ring hydroxylating dioxygenase) Baldwin et al., 2003 Benzyl-succinate synthase COO- PHE (Phenol hydroxylases)CHBaldwin 3 et al., 2003 bssA CH TMO (Toluene monooxygenase) Hendrickx et al., CH 2006 2 COO- BssA (Benzyl-succinate synthase) Howard Junca, personal communication Adapted from Kahng et al., 2001
CATABOLIC ARRAY Tol plasmid-like Xylene MO bcrA T. aromatica Catechol-2,3- bssA dioxygenase G4 B. Magnetospirillum vietnamensis sp. TS6 Catechol-2,3- dioxygenase Soluble diiron MO Vilchez-Vargas et al. 2012. Environ. Microbiol. in press.
The catabolic array indicates that monooxygenation seems to be the predominant mechanism for aerobic toluene degradation in PFRs Only in PFR 6, the anaerobic toluene degradation seems to have a significant contribution How can we confirm these results?.... ...the old fashion way: Isolation
AEROBIC ISOLATES Pseudomonas sp. AET-5-01 CH3 CH2OH Isolated from PFR5 (Baldwin BR., et al., 2003) CH3 CH3 Ralstonia pickettii AET-6-14 Isolated from PFR6 OH (Hendrickx B., et al., 2006a,b) CH3 CH3 OH Pseudomonas sp. AET-6-18 H H Isolated from PFR6 OH (Hendrickx B., et al., 2006a,b)
Screening with degenerate primers using cDNA as template Note: The cDNA was prepared using the reverse primer of each primer pair because with hexamer primers we couldn’t detect get any PCR product BssA (benzylsuccinate synthase) Most of the DNA bssA -357 clones were very -357 -134 -134 256 247 -79 247 256 mV -79 -14 R6 -14 87 45 R5 45 87 C+ 75 75 closely related to C- Magnetospirillum sp. TS-6 (around 90 from 93 clones) RT+ RT- RT+ RT- R5 R6 C+:T aromatica
Where do we go from here?
UBT papers: POF III: Controlling Chemicals’ Fate (CCF) Towards eco-compatible chemicals: Managing ecosystem chemodynamics
Linking water and soil research: Multiphasic process analysis in Planted Fixed- Bed Reactors (PFR) Temporal Fluctuations Microbial Adaptations Microbial Community & Catabolism - Metagenomics - Lipidomics (UBT) - Metagenomics (UBT, HZI) (UBT, HZI) - Transcript Analysis (UBT) - Protein SIP (PROTEOM) - 2D Isotope Fractionation (ISOBIO) - Physiology (UBT) - Isolation (UBT) Pollutant e.g. toluene as a model compound; pharmaceuticals, rhizospheric health care products effects Wießner et al. 2005. Water Res.
Investigations planned with the planted fixed-bed reactors (PFR) within Workpackage 2 of CCF (POF3) Degradation of a pollutants such as toluene or e.g. ibuprofen or paracetamol in at least two PFRs. Elucidation of the microbiota responsible for the degradation under aerobic and anaerobic conditions. Analysis of two-dimensional isotope fractionation in order to elucidate the catabolic pathways. Detection of the catabolic genes responsible for the degradation. This will be done by metagenomic and clone library techniques as well as by applying a catabolic gene array developed by the HZI. The expression of these catabolic genes will be systematically analyzed under seasonal (winter-spring-summer-autumn) as well as diurnal (day- night) cycles. Addition of the compounds in form of the 13C-labelled stable isotopes. Monitoring of the development of microbial and catabolic diversity by protein-based stable isotope probing (protein SIP).
Potential pharmaceuticals to be investigated Paracetamol Ibuprofen
More technical activities
Future Research Questions for CWs Effect of filter material additives gravel, + activated carbon, + ferric iron Performance efficiency of CW types gravel filter system vs. plant mat Integ. Contaminant massbalance microbial degradation, plant uptake, emission Technical approach for promoting removal efficiency Filter material additives: Plant mat without gravel Mass balance incl. emission
Constructed wetland efficiencies - Benzene Comparison of wetland type: planted gravel filter vs. plant mat planted filter bed plant mat 100 80 Plant mat without gravel residual load [%-inflow] 60 benzene 40 20 0 1.6.07 1.10.07 1.2.08 1.6.08 1.10.08 1.2.09 1.6.09 Seeger et al. 2011, Environ. Poll. 159, 3769-3776
Nitrogen transformation processes N2 NH4+ Tools: [NH2OH] Isotope fractionation, S0 FISH, qPCR NO N 2O NO NO2- NO2- NH4+ NO3- CWs have favorable conditions H 2S for partial nitrification and anammox Corg
Removal mechanisms of pathogenic germs in CWs Hygienisation Protozoa Bacteriophages Bdellevibrio Plants lawrence-throughthevisor.blogspot.com Main future applications of CWs will be the treatment of domestic sewage in countries such as China, India, Vietnam, etc. EU project: Water4crops
Acknowledgements Peter Kuschk Arndt Wiessner Uwe Kappelmeyer Jochen A. Müller Matthias Kästner Paula Martínez Lavanchy Zhongbing Chen Vianey Marín Cevada Luciana Schultze Nobre Mareike Braeckevelt Eva M. Seeger Alexander Al-Dahoodi Helga Fazekas Otoniel Carranza Jaime Nivala ANA/UBT and many more colleagues! Fabio Kraft Anja Taubert Ilja Iwlew Claudia Pietsch Kerstin Puschendorf Ines Mäusezahl Kerstin Ethner Ivonne Nijenhuis ISOBIO Jana Seifert PROTEOM Monika Möder ANA Thank you for your attention!
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