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Crone BC, Sorial GA, Pressman JG, Ryu H, Keely SP, Brinkman N, Bennett-Stamper C, Garland JL. Design and evaluation of degassed anaerobic membrane biofilm reactors for improved methane recovery. BIORESOURCE TECHNOLOGY REPORTS 2020; 10:100407. [PMID: 33015594 PMCID: PMC7529100 DOI: 10.1016/j.biteb.2020.100407] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Abstract] [Key Words] [Grants] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/23/2022]
Abstract
Anaerobic treatment of domestic wastewater (DWW) produces dissolved methane that needs to be recovered for use as an energy product. Membrane-based recovery systems have been reported in the literature but are often limited by fouling. The objective of this study was to develop a methane producing biofilm on the shell side surface a membrane to allow for immediate recovery of methane as it was produced, negating mass transfer resistance caused by fouling. Between 89 and 96% of total methane produced was recovered via in-situ degassing without the need for fouling control or cleaning throughout 72 weeks of operation. High methane recovery efficiencies led to predictions of net positive energy yield in one reactor and a 32-61% reduction in energy demand in the others compared to the control. This research demonstrates the feasibility and usefulness of combining attached growth anaerobic wastewater treatment processes with hollow fiber membrane methane recovery systems for improved operation.
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Affiliation(s)
- Brian C Crone
- United States Environmental Protection Agency, Office of Research and Development, Center for Environmental Solutions and Emergency Response, United States of America
| | - George A Sorial
- Department of Chemical and Environmental Engineering, University of Cincinnati, United States of America
| | - Jonathan G Pressman
- United States Environmental Protection Agency, Office of Research and Development, Center for Environmental Solutions and Emergency Response, United States of America
| | - Hodon Ryu
- United States Environmental Protection Agency, Office of Research and Development, Center for Environmental Solutions and Emergency Response, United States of America
| | - Scott P Keely
- United States Environmental Protection Agency, Office of Research and Development, Center for Environmental Solutions and Emergency Response, United States of America
| | - Nichole Brinkman
- United States Environmental Protection Agency, Office of Research and Development, Center for Environmental Solutions and Emergency Response, United States of America
| | - Christina Bennett-Stamper
- United States Environmental Protection Agency, Office of Research and Development, Center for Environmental Solutions and Emergency Response, United States of America
| | - Jay L Garland
- United States Environmental Protection Agency, Office of Research and Development, Center for Environmental Solutions and Emergency Response, United States of America
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2
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Louca S, Scranton MI, Taylor GT, Astor YM, Crowe SA, Doebeli M. Circumventing kinetics in biogeochemical modeling. Proc Natl Acad Sci U S A 2019; 116:11329-11338. [PMID: 31097587 PMCID: PMC6561284 DOI: 10.1073/pnas.1819883116] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/18/2022] Open
Abstract
Microbial metabolism drives biogeochemical fluxes in virtually every ecosystem. Modeling these fluxes is challenged by the incredible diversity of microorganisms, whose kinetic parameters are largely unknown. In poorly mixed systems, such as stagnant water columns or sediments, however, long-term bulk microbial metabolism may become limited by physical transport rates of substrates across space. Here we mathematically show that under these conditions, biogeochemical fluxes are largely predictable based on the system's transport properties, chemical boundary conditions, and the stoichiometry of metabolic pathways, regardless of the precise kinetics of the resident microorganisms. We formalize these considerations into a predictive modeling framework and demonstrate its use for the Cariaco Basin subeuphotic zone, one of the largest anoxic marine basins worldwide. Using chemical concentration data solely from the upper boundary (depth 180 m) and lower boundary (depth 900 m), but without a priori knowledge of metabolite fluxes, chemical depth profiles, kinetic parameters, or microbial species composition, we predict the concentrations and vertical fluxes of biologically important substances, including oxygen, nitrate, hydrogen sulfide, and ammonium, across the entire considered depth range (180-900 m). Our predictions largely agree with concentration measurements over a period of 14 years ([Formula: see text] = 0.78-0.92) and become particularly accurate during a period where the system was near biogeochemical steady state (years 2007-2009, [Formula: see text] = 0.86-0.95). Our work enables geobiological predictions for a large class of ecosystems without knowledge of kinetic parameters or geochemical depth profiles. Conceptually, our work provides a possible explanation for the decoupling between microbial species composition and bulk metabolic function, observed in various ecosystems.
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Affiliation(s)
- Stilianos Louca
- Institute of Ecology and Evolution, University of Oregon, Eugene, OR 97403;
- Department of Biology, University of Oregon, Eugene, OR 97403
| | - Mary I Scranton
- School of Marine and Atmospheric Sciences, Stony Brook University, Stony Brook, NY 11794
| | - Gordon T Taylor
- School of Marine and Atmospheric Sciences, Stony Brook University, Stony Brook, NY 11794
| | - Yrene M Astor
- Estación de Investigaciones Marinas de Margarita, Fundación La Salle de Ciencias Naturales, Punta de Piedras, Estado Nueva Esparta, Venezuela
- Institute for Marine Remote Sensing, University of South Florida, Tampa, FL 33701
| | - Sean A Crowe
- Department of Microbiology and Immunology, University of British Columbia, Vancouver, BC V6T 1Z3, Canada
- Department of Earth, Ocean, and Atmospheric Sciences, University of British Columbia, Vancouver, BC V6T 1Z4, Canada
| | - Michael Doebeli
- Biodiversity Research Centre, University of British Columbia, Vancouver, BC V6T 1Z4, Canada
- Department of Mathematics, University of British Columbia, Vancouver, BC V6T 1Z2, Canada
- Department of Zoology, University of British Columbia, Vancouver, BC V6T 1Z4, Canada
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Effect of Tidal Cycling Rate on the Distribution and Abundance of Nitrogen-Oxidizing Bacteria in a Bench-Scale Fill-and-Drain Bioreactor. WATER 2018. [DOI: 10.3390/w10040492] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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Ye Y, Saikaly PE, Logan BE. Simultaneous nitrogen and organics removal using membrane aeration and effluent ultrafiltration in an anaerobic fluidized membrane bioreactor. BIORESOURCE TECHNOLOGY 2017; 244:456-462. [PMID: 28800555 DOI: 10.1016/j.biortech.2017.07.183] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 06/24/2017] [Revised: 07/28/2017] [Accepted: 07/29/2017] [Indexed: 06/07/2023]
Abstract
Dissolved methane and a lack of nutrient removal are two concerns for treatment of wastewater using anaerobic fluidized bed membrane bioreactors (AFMBRs). Membrane aerators were integrated into an AFMBR to form an aeration membrane fluidized bed membrane bioreactor (AeMFMBR) capable of simultaneous removal of organic matter and ammonia without production of dissolved methane. Good effluent quality was obtained with no detectable suspended solids, 93±5% of chemical oxygen demand (COD) removal to 14±11mg/L, and 74±8% of total ammonia (TA) removal to 12±3mg-N/L for domestic wastewater (COD of 193±23mg/L and TA of 49±5mg-N/L) treatment. Nitrate and nitrite concentrations were always low (<1mg-N/L) during continuous flow treatment. Membrane fouling was well controlled by fluidization of the granular activated carbon (GAC) particles (transmembrane pressures maintained <3kPa). Analysis of the microbial communities suggested that nitrogen removal was due to nitrification and denitrification based on the presence of microorganisms associated with these processes.
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Affiliation(s)
- Yaoli Ye
- Department of Civil and Environmental Engineering, The Pennsylvania State University, University Park, PA 16802, United States
| | - Pascal E Saikaly
- Biological and Environmental Sciences and Engineering Division, King Abdullah University of Science and Technology (KAUST), 4700 King Abdullah Boulevard, Thuwal 23955-6900, Saudi Arabia
| | - B E Logan
- Department of Civil and Environmental Engineering, The Pennsylvania State University, University Park, PA 16802, United States.
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Wang L, Zheng P, Xing Y, Li W, Yang J, Abbas G, Liu S, He Z, Zhang J, Zhang H, Lu H. Effect of particle size on the performance of autotrophic nitrogen removal in the granular sludge bed reactor and microbiological mechanisms. BIORESOURCE TECHNOLOGY 2014; 157:240-6. [PMID: 24561629 DOI: 10.1016/j.biortech.2014.01.116] [Citation(s) in RCA: 18] [Impact Index Per Article: 1.8] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 11/13/2013] [Revised: 01/24/2014] [Accepted: 01/28/2014] [Indexed: 05/27/2023]
Abstract
The effect of particle size on the performance of autotrophic nitrogen removal in the granular sludge bed reactor (GSB-ANR) and microbiological mechanisms were investigated. The results indicated that performance of GSB-ANR process decreased gradually with the increase of the granular sludge size. Indeed small granules ranging between 0.5 and 0.9mm had a higher nitrogen removal capacity than large ones. The reasons of this effect were that (i) the aerobic ammonium oxidizing capacity of microorganisms was the bottle neck of nitrogen removal in GSB-ANR process, and the increase of aerobic ammonium oxidizing activity enhances nitrite production in nitrification and promotes subsequent nitrite consumption during anaerobic ammonia oxidation; (ii) the aerobic/anaerobic zone separation in granular sludge was the key factor affecting the aerobic ammonium oxidizing capacity of microorganisms. The small granules had a larger aerobic functional zone (75.1%) which was profitable for up-regulating the expression level of functional gene in aerobic ammonium oxidizing microorganisms.
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Affiliation(s)
- Lan Wang
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
| | - Ping Zheng
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China.
| | - Yajuan Xing
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
| | - Wei Li
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
| | - Jian Yang
- State Key Laboratory of Plant Physiology and Biochemistry, College of Life Science, Zhejiang University, Hangzhou 310058, China
| | - Ghulam Abbas
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China; Department of Chemical Engineering, University of Gujrat, Gujrat, Pakistan
| | - Shuai Liu
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
| | - Zhanfei He
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
| | - Jiqiang Zhang
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
| | - Hongtao Zhang
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
| | - Huifeng Lu
- Department of Environmental Engineering, Zhejiang University, Hangzhou 310058, China
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Martin KJ, Nerenberg R. The membrane biofilm reactor (MBfR) for water and wastewater treatment: principles, applications, and recent developments. BIORESOURCE TECHNOLOGY 2012; 122:83-94. [PMID: 22541953 DOI: 10.1016/j.biortech.2012.02.110] [Citation(s) in RCA: 181] [Impact Index Per Article: 15.1] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 11/09/2011] [Revised: 02/25/2012] [Accepted: 02/27/2012] [Indexed: 05/31/2023]
Abstract
The membrane biofilm reactor (MBfR), an emerging technology for water and wastewater treatment, is based on pressurized membranes that supply a gaseous substrate to a biofilm formed on the membrane's exterior. MBfR biofilms behave differently from conventional biofilms due to the counter-diffusion of substrates. MBfRs are uniquely suited for numerous treatment applications, including the removal of carbon and nitrogen when oxygen is supplied, and reduction of oxidized contaminants when hydrogen is supplied. Major benefits include high gas utilization efficiency, low energy consumption, and small reactor footprints. The first commercial MBfR was recently released, and its success may lead to the scale-up of other applications. MBfR development still faces challenges, including biofilm management, the design of scalable reactor configurations, and the identification of cost-effective membranes. If future research and development continue to address these issues, the MBfR may play a key role in the next generation of sustainable treatment systems.
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Affiliation(s)
- Kelly J Martin
- Department of Civil Engineering and Geological Sciences, University of Notre Dame, 156 Fitzpatrick Hall, Notre Dame, IN 46556, USA.
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7
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McLamore ES, Zhang W, Porterfield DM, Banks MK. Membrane-aerated biofilm proton and oxygen flux during chemical toxin exposure. ENVIRONMENTAL SCIENCE & TECHNOLOGY 2010; 44:7050-7057. [PMID: 20735036 DOI: 10.1021/es1012356] [Citation(s) in RCA: 17] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 05/29/2023]
Abstract
Bioreactors containing sessile bacteria (biofilms) grown on hollow fiber membranes have been used for treatment of many wastestreams. Real time operational control of bioreactor performance requires detailed knowledge of the relationship between bulk liquid water quality and physiological transport at the biofilm-liquid interface. Although large data sets exist describing membrane-aerated bioreactor effluent quality, very little real time data is available characterizing boundary layer transport under physiological conditions. A noninvasive, microsensor technique was used to quantify real time (≈1.5 s) changes in oxygen and proton flux for mature Nitrosomonas europaea and Pseudomonas aeruginosa biofilms in membrane-aerated bioreactors following exposure to environmental toxins. Stress response was characterized during exposure to toxins with known mode of action (chlorocarbonyl cyanide phenyl-hydrazone and potassium cyanide), and four environmental toxins (rotenone, 2,4-dinitrophenol, cadmium chloride, and pentachlorophenol). Exposure to sublethal concentrations of all environmental toxins caused significant increases in O(2) and/or H(+) flux (depending on the mode of action). These real time microscale signatures (i.e., fingerprints) of O(2) and H(+) flux can be coupled with bulk liquid analysis to improve our understanding of physiology in counter-diffusion biofilms found within membrane aerated bioreactors; leading to enhanced monitoring/modeling strategies for bioreactor control.
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Affiliation(s)
- E S McLamore
- Physiological Sensing Facility, Purdue University, 1203 West State Street, West Lafayette, Indiana 47907-2057, USA.
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Terada A, Ito J, Matsumoto S, Tsuneda S. Fibrous Support Stabilizes Nitrification Performance of a Membrane-Aerated Biofilm: The Effect of Liquid Flow Perturbation. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN 2009. [DOI: 10.1252/jcej.09we032] [Citation(s) in RCA: 9] [Impact Index Per Article: 0.6] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/11/2022]
Affiliation(s)
- Akihiko Terada
- Department of Environmental Engineering, Technical University of Denmark
| | - Junpei Ito
- Department of Chemical Engineering, Waseda University
| | - Shinya Matsumoto
- Department of Life Science and Medical Bioscience, Waseda University
| | - Satoshi Tsuneda
- Department of Life Science and Medical Bioscience, Waseda University
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