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Moving bed biofilm reactor

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K1 MBBR carrier with biofilm

Moving bed biofilm reactor (MBBR) is a type of wastewater treatment process that was first invented by Professor Hallvard Ødegaard at Norwegian University of Science and Technology in the late 1980s.[1] The process takes place in an aeration tank with plastic carriers that a biofilm can grow on. The compact size and cheap wastewater treatment costs offers many advantages for the system. The main objective of using MBBR being water reuse and nutrient removal or recovery.[2] In theory, wastewater will be no longer considered waste, it can be considered a resource.

Background

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Overview

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Due to early issues with biofilm reactors, like hydraulic instability and uneven biofilm distribution, moving bed biofilm technology was developed.[3] The MBBR system consists of an aeration tank (similar to an activated sludge tank) with special plastic carriers that provide a surface where a biofilm can grow. There is a wide variety of plastic carriers used in these systems. These carriers vary in surface area and in shape, each offering different advantages and disadvantages. Surface area plays a very important role in biofilm formation. Free-floating carriers allow biofilms to form on the surface, therefore a large internal surface area is crucial for contact with water, air, bacteria, and nutrients.[4] The carriers will be mixed in the tank by the aeration system and thus will have good contact between the substrate in the influent wastewater and the biomass on the carriers.[5] The most preferable material is currently high density polyethylene (HDPE) due to its plasticity, density, and durability. [citation needed]

To achieve higher concentration of biomass in the bioreactors, hybrid MBBR systems have been used where suspended and attached biomass co-exist contributing both to biological processes.[6] Additionally, there are anaerobic MBBRs that have been mainly used for industrial wastewater treatment.[7] A 2019 article described a combination of anaerobic (methanogenic) MBBR with aerobic MBBR that was applied in a municipal wastewater treatment laboratory, with simultaneous production of biogas.[8]

History

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The development of MBBR technology is attributed to Professor Hallvard Ødegaard and his colleagues at Norwegian University of Science and Technology (NTNU). This is traced back to the late 1970s to early 1980s. The first MBBR pilot plant was installed at NTNU in the early 1980s in which its success lead to the construction and start-up of the first full-scale MBBR plant in Norway in 1985.[9] It was commercialized by Kaldnes Miljöteknologi (now called AnoxKaldnes and owned by Veolia Water Technologies). Since then, MBBR technology has been widely adopted throughout the world, mainly in Europe and Asia. Now, there are over 700 wastewater treatment systems (both municipal and industrial) installed in over 50 countries.[10]

Current Usage

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Today, MBBR technology is used for municipal sewage treatment, industrial wastewater treatment, and decentralized wastewater treatment. This technology has been used in many different industries, some of them being:[citation needed]

  • Automotive industry
  • Chemical industry
  • Food and beverage
  • Metal plating and finishing

The MBBR system is considered a biofilm or biological process, not a chemical or mechanical process. Other conventional biofilm processes for wastewater treatment are called trickling filter, rotating biological contactor (RBC) and biological aerated filter (BAF).

Important applications:[11]

Methods

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There are many design components of MBBR that come together to make the technology highly efficient. First, the process occurs in a basin (or aeration tank). The overall size of this tank is dependent on both the type and volume of wastewater being processed. The influent enters the basin at the beginning of treatment. Second component being the media. The media consists of the free-floating biocarriers mentioned earlier and can occupy as much as 70 percent of the tank. Third, an aeration grid is responsible for helping the media move through the basin and ensure the carriers come into contact with as much waste as possible, in addition to introducing more oxygen into the basin. Lastly, a sieve keeps all the carriers in the tank to prevent the plastic carriers from escaping the aeration.[12]

Though there are a few different methods, they all use the same design components. The continuous flow method involves continuous flow of wastewater into the basin, with an equal flow of treated water exiting through the sieve. Intermittent aeration method operating in cycles of aeration and non-aeration, allowing for both aerobic conditions and anoxic conditions.[13] Sequencing batch reactor (SBR) method is completed in a single reactor where several treatment steps occur in a sequence, where the treated water is removed before the cycle begins again.[14] Large diameter submersible mixers are commonly used as a method for mixing in these systems.

Removal of Micropollutants

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Moving bed biofilm reactors have shown promising results to remove micropollutations (MPs) from wastewater.[15][16][17][18] MPs fall into several groups of chemicals such as pharmaceuticals, organophosphorus pesticides (OPs), care products and endocrine disruptors.[19] A 2012 article reported described the use of MBBR technology to remove pharmaceuticals such as beta-blockers, analgesics, anti-depressants, and antibiotics from hospital wastewater.[20][16] Moreover, application of MBBR as a biological technique combined with chemical treatment has attracted a great deal of attention for removal of organophosphorous pesticide from wastewater.[21] The advantage of MBBRs can be associated with its high solid retention time, which allows the proliferation of slow-growing microbial communities with multiple functions in biofilms. The dynamics of such microbial communities greatly depends on organic loading in MBBR systems.[22]

Moving bed biofilm reactors can efficiently treat hospital wastewater and remove pharmaceutical micropollutants. A 2023 study has shown that a strictly anaerobic MBBR, combined with an aerobic biofilm reactor can achieve high removal rates of pharmaceuticals, such as metronidazole, trimethoprim, sulfamethoxazole, and valsartan.[23]

Advantages

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Biofilm processes in general require less space than activated sludge systems because the biomass is more concentrated, and the efficiency of the system is less dependent on the final sludge separation.[citation needed]

MBBR systems do not need a recycling of the sludge, which is the case with activated sludge systems.

The MBBR system is often installed as a retrofit of existing activated sludge tanks to increase the capacity of the existing system. The degree of filling of carriers can be adapted to the specific situation and the desired capacity. Thus an existing treatment plant can increase its capacity without increasing the footprint by constructing new tanks.

Some other advantages are:

  • Increased performance and volumetric treatment capacity[3]
  • Higher effective sludge retention time (SRT) which is favorable for nitrification
  • Responds to load fluctuations without operator intervention
  • Lower sludge production
  • Less area required
  • Resilient to toxic shock
  • Process performance independent of secondary clarifier (due to the fact that there is no sludge return line).[24]

Disadvantages

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A disadvantage with other biofilm processes is that they experience bioclogging and build-up of headloss.[1] Depending on the type of waste and design of the process, several problems can occur during the full-scale process. Some of the disadvantages are:[25]

  • Feed pipe/effluent sieve blocking
  • Nonhomogeneous mixing
  • Carrier voids blocking
  • Destroyed carriers
  • Carriers accumulating at the effluent sieves
  • Carrier overflow

Alternative Wastewater Treatment Systems

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There are many alternative wastewater treatment systems that can be used in place of MBBRs. The selection of the appropriate system depends on the wastewater coming in, treatment objectives, available space, and budgets.

Some other options are:

See also

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References

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  1. ^ a b Ødegaard, H.; Rusten, B.; Westrum, T. (October 1994). "A new moving bed biofilm reactor - applications and results". Water Science and Technology. 29 (10–11): 157–165. doi:10.2166/wst.1994.0757.
  2. ^ Leyva-Díaz, J. C.; Monteoliva-García, A.; Martín-Pascual, J.; Munio, M. M.; García-Mesa, J. J.; Poyatos, J. M. (2020-03-01). "Moving bed biofilm reactor as an alternative wastewater treatment process for nutrient removal and recovery in the circular economy model". Bioresource Technology. 299: 122631. doi:10.1016/j.biortech.2019.122631. ISSN 0960-8524.
  3. ^ a b di Biase, Alessandro; Kowalski, Maciej S.; Devlin, Tanner R.; Oleszkiewicz, Jan A. (2019-10-01). "Moving bed biofilm reactor technology in municipal wastewater treatment: A review". Journal of Environmental Management. 247: 849–866. doi:10.1016/j.jenvman.2019.06.053. ISSN 0301-4797.
  4. ^ di Biase, Alessandro; Kowalski, Maciej S.; Devlin, Tanner R.; Oleszkiewicz, Jan A. (2019-10-01). "Moving bed biofilm reactor technology in municipal wastewater treatment: A review". Journal of Environmental Management. 247: 849–866. doi:10.1016/j.jenvman.2019.06.053. ISSN 0301-4797.
  5. ^ Ødegaard, Hallvard (2012). Vann- og Avløpsteknikk [Water and Drainage Technology] (in Norwegian). Hamar, NO: Norsk Vann (Norwegian Water). ISBN 9788241403361.[page needed]
  6. ^ Mazioti, Aikaterini A.; Stasinakis, Athanasios S.; Psoma, Aikaterini K.; Thomaidis, Nikolaos S.; Andersen, Henrik R. (February 2017). "Hybrid Moving Bed Biofilm Reactor for the biodegradation of benzotriazoles and hydroxy-benzothiazole in wastewater" (PDF). Journal of Hazardous Materials. 323 (Pt A): 299–310. doi:10.1016/j.jhazmat.2016.06.035. PMID 27396311. S2CID 25314327.
  7. ^ di Biase, A.; Devlin, T.R.; Kowalski, M.S.; Oleszkiewicz, J.A. (June 2018). "Performance and design considerations for an anaerobic moving bed biofilm reactor treating brewery wastewater: Impact of surface area loading rate and temperature". Journal of Environmental Management. 216: 392–398. doi:10.1016/j.jenvman.2017.05.093. PMID 28595913. S2CID 25584756.
  8. ^ Kora, Elianta; Theodorelou, Danai; Gatidou, Georgia; Fountoulakis, Michail S.; Stasinakis, Athanasios S. (September 2019). "Removal of polar micropollutants from domestic wastewater using a methanogenic—aerobic Moving Bed Biofilm Reactor system". Chemical Engineering Journal. 382: 122983. doi:10.1016/j.cej.2019.122983. S2CID 204112754.
  9. ^ Ødegaard, H. (2019), "MBBR and IFAS systems", Advances in Wastewater Treatment, IWA Publishing, doi:10.2166/9781780409719_0101, ISBN 978-1-78040-971-9, retrieved 2023-05-01
  10. ^ Vann- og avløpsteknikk. Hallvard Ødegaard, Norsk Vann BA. Hamar: Norsk Vann. 2012. ISBN 978-82-414-0336-1. OCLC 939782945.{{cite book}}: CS1 maint: others (link)
  11. ^ "Moving Bed Biofilm Reactor (MBBR) » Ecologix Systems". Ecologix Systems. Retrieved 2023-05-01.
  12. ^ Frankel, Tom (2019-11-21). "What Is MBBR Wastewater Treatment & How Does It Work? | SSI". SSI Aeration. Retrieved 2023-05-01.
  13. ^ Luan, Ya-Nan; Yin, Yue; An, Yuning; Zhang, Feng; Wang, Xiaodong; Zhao, Fangchao; Xiao, Yihua; Liu, Changqing (2022-08-01). "Investigation of an intermittently-aerated moving bed biofilm reactor in rural wastewater treatment under lowdissolved oxygen and C/N condition". Bioresource Technology. 358: 127405. doi:10.1016/j.biortech.2022.127405. ISSN 0960-8524.
  14. ^ Kamble, Buddham; Shaha, Sunil (June 2020). "Wastewater Treatment by Moving Bed Sequencing Batch Reactor (MBSBR): A Review" (PDF). International Research Journal of Engineering and Technology (IRJET). 07 (06).
  15. ^ Tang, Kai; Rosborg, Peter; Rasmussen, Emma S; Hambly, Adam; Madsen, Michael; Jensen, Niels M; Hansen, Aviaja A; Sund, Christina; Andersen, Heidi G; Torresi, Elena; Kragelund, Caroline (2021-02-05). "Impact of intermittent feeding on polishing of micropollutants by moving bed biofilm reactors (MBBR)". Journal of Hazardous Materials. 403: 123536. doi:10.1016/j.jhazmat.2020.123536. ISSN 0304-3894. PMID 32823027. S2CID 221238674.
  16. ^ a b Casas, Mònica Escolà; Chhetri, Ravi Kumar; Ooi, Gordon; Hansen, Kamilla M. S.; Litty, Klaus; Christensson, Magnus; Kragelund, Caroline; Andersen, Henrik R.; Bester, Kai (2015-10-15). "Biodegradation of pharmaceuticals in hospital wastewater by staged Moving Bed Biofilm Reactors (MBBR)". Water Research. 83: 293–302. doi:10.1016/j.watres.2015.06.042. ISSN 0043-1354. PMID 26164801.
  17. ^ Mazioti, Aikaterini A.; Stasinakis, Athanasios S.; Psoma, Aikaterini K.; Thomaidis, Nikolaos S.; Andersen, Henrik R. (2017-02-05). "Hybrid Moving Bed Biofilm Reactor for the biodegradation of benzotriazoles and hydroxy-benzothiazole in wastewater". Journal of Hazardous Materials. Special Issue on Emerging Contaminants in engineered and natural environment. 323 (Pt A): 299–310. doi:10.1016/j.jhazmat.2016.06.035. ISSN 0304-3894. PMID 27396311. S2CID 25314327.
  18. ^ Polesel, Fabio; Torresi, Elena; Loreggian, Luca; Casas, Mònica Escolà; Christensson, Magnus; Bester, Kai; Plósz, Benedek Gy. (2017-10-15). "Removal of pharmaceuticals in pre-denitrifying MBBR—Influence of organic substrate availability in single- and three-stage configurations". Water Research. 123: 408–419. doi:10.1016/j.watres.2017.06.068. ISSN 0043-1354. PMID 28689125. S2CID 205700311.
  19. ^ Nödler, Karsten; Voutsa, Dimitra; Licha, Tobias (August 2014). "Polar organic micropollutants in the coastal environment of different marine systems". Marine Pollution Bulletin. 85 (1): 50–59. doi:10.1016/j.marpolbul.2014.06.024. ISSN 0025-326X. PMID 25015017.
  20. ^ Falås, P.; Baillon-Dhumez, A.; Andersen, H. R.; Ledin, A.; la Cour Jansen, J. (2012-03-15). "Suspended biofilm carrier and activated sludge removal of acidic pharmaceuticals". Water Research. 46 (4): 1167–1175. doi:10.1016/j.watres.2011.12.003. ISSN 0043-1354. PMID 22209263.
  21. ^ Chen, Sheng; Sun, Dezhi; Chung, Jong-Shik (2007-06-01). "Treatment of pesticide wastewater by moving-bed biofilm reactor combined with Fenton-coagulation pretreatment". Journal of Hazardous Materials. 144 (1): 577–584. doi:10.1016/j.jhazmat.2006.10.075. ISSN 0304-3894. PMID 17141410.
  22. ^ Nogueira, Regina; Melo, Luı́s F; Purkhold, Ulrike; Wuertz, Stefan; Wagner, Michael (January 2002). "Nitrifying and heterotrophic population dynamics in biofilm reactors: effects of hydraulic retention time and the presence of organic carbon". Water Research. 36 (2): 469–481. doi:10.1016/S0043-1354(01)00229-9. hdl:1822/1602. PMID 11827353.
  23. ^ Iliopoulou, Athanasia; Arvaniti, Olga S.; Deligiannis, Michalis; Gatidou, Georgia; Vyrides, Ioannis; Fountoulakis, Michalis S.; Stasinakis, Athanasios S. (2023-10-01). "Combined use of strictly anaerobic MBBR and aerobic MBR for municipal wastewater treatment and removal of pharmaceuticals". Journal of Environmental Management. 343: 118211. doi:10.1016/j.jenvman.2023.118211. ISSN 0301-4797.
  24. ^ Burton, Franklin; Tchobanoglous, George; Tsuchihashi, Ryujiro; Stensel, H. David; Metcalf & Eddy (2013-09-03). Wastewater Engineering: Treatment and Resource Recovery. McGraw-Hill Education. ISBN 9780073401188.[page needed]
  25. ^ Wang, Shuai; Parajuli, Sudeep; Sivalingam, Vasan; Bakke, Rune (2019-08-08). Biofilm in Moving Bed Biofilm Process for Wastewater Treatment. IntechOpen. ISBN 978-1-78985-900-3.
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