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Denitrification with dissolved methane in an MBR after a methanogenic pre-treatment at ambient temperaturePaetkau, M., Cicek, N. 2011. Comparison of nitrogen removal and sludge characteristics between aconventional and a simultaneous nitrification-denitrification membrane bioreactor. Desalination283, 165-168.Park, S., Lee, C.-H., Ryu, C.-R., Sung, K. 2009. Biofiltration for reducing methane emissions frommodern sanitary landfills at the low methane generation stage. Water, Air, and Soil Pollution196(1), 19–27.Raghoebarsing, A.A., Pol, A., van de Pas-Schoonen, K.T., Smolders, A.J.P., Ettwig, K.F., Rijpstra,I.C., Schouten, S., Sinninghe Damste, J.S., Op den Camp, H.J.M., Jetten, M.S.M., Strous, M.2006. A microbial consortium couples anaerobic methane oxidation to denitrification. Nature440, 918–921.Rajapakse, J.P., Scutt, J. E. 1999. Denitrification with natural gas and various new growth media.Water Research 33(18), 3723-3734.Rhee G. and Fuhs G. (1978) Wastewater denitrification with one-carbon compounds as energysource. Journal of the Water Pollution Control Federation 50(9), 2111-2119.Sánchez, A., Buntner, D., Garrido, J.M. 2013. Impact of methanogenic pre-treatment on theperformance of an aerobic MBR system. Water Research 47, 1229-1236.Sander, R. 1999. Compilation of Henry’s Law Constants for Inorganic and Organic Species ofPotential Importance in Environmental Chemistry, http://www.rolf-sander.net/henry/.Shen, Z., Zhou, Y., Hu, J., Wang, J. 2013. Denitrification performance and microbial diversity in apacked-bed bioreactor using biodegradable polymer as carbon source and biofilm support.Journal of Hazardous Materials 250-251, 431-438.Souza, C.L., Chernicharo, C.A.L., Aquino, S.F. 2011. Quantification of dissolved methane in UASBreactors treating domestic wastewater under different operating conditions. Water Science andTechnology 64(11), 2259-2265.Thalasso, F., Vallecillo, A., García-Encina, P., Fernández-Polanco, F. 1997. The use of methane asa sole carbon source for wastewater denitrification. Water Research 31(1), 55–60.Valentine, D.L., Reeburgh, W.S. 2000. New perspectives on anaerobic methane oxidation.Environmental Microbiology 2(5), 477-484.van Haandel, A. C., Lettinga, G. 1994. Anaerobic Sewage Treatment – A Practical Guide forRegions with a Hot Climate. John Wiley & Sons Ltd, Chichester, UK.van Lier, J.B. 2008. High-rate anaerobic wastewater treatment: diversifying from end-of-the-pipetreatment to resource-oriented conversion techniques. Water Science and Technology 57(8),1137-1149.van't Riet, K., Tramper, J. 1991. Basic Bioreactor Design. Marcel Dekker Inc., New York-Basel.Waki, M., Yasuda, T., Yokoyama, H., Hanajima, D., Ogino, A., Suzuki, K., Yamagishi, T., Suwa, Y.,Tanaka, Y. 2009. Nitrogen removal by co-occurring methane oxidation, denitrification, aerobicammonium oxidation, and anammox. Applied Microbiology and Biotechnology 84(5), 977-985.Wen, X., Bu, Q., Huang, X. 2004. Study on fouling characteristic of axial hollow fibers cross-flowmicrofiltration under different flux operations, in: Proceedings of the Water Environment-Membrane Technology Conference, Seoul, Korea.171
Chapter 6Wu, Ming L. 2012. Cell biology and biochemistry of the denitrifying methanotroph “CandidatusMethylomirabilis oxyfera”. Radboud University Nijmegen (The Netherlands), ISBN: 978-94-6191-408-8.172
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UNIVERSIDAD DE SANTIAGO DE COMPOSTE
Page 6 and 7:
padres Macario y Marisa, les agrade
Page 8 and 9:
2.1.2. Nitrogen compounds 662.1.2.1
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Chapter 4: Combining UASB and MBR f
Page 14 and 15:
Objetivos y resumenEsta tesis se en
Page 16 and 17:
Objetivos y resumenpermeabilidad de
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Objetivos y resumenuno de los pará
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Objetivos y resumenel sistema propu
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Objetivos y resumenconcentraciones
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Obxectivos e resumoauga tratada. O
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Obxectivos e resumoNo Capítulo 3,
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Obxectivos e resumog·L -1 , valore
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Obxectivos e resumoparámetros clav
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Objectives and summaryThis thesis i
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Objectives and summaryOn the basis
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Objectives and summaryfrom the MBR
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Objectives and summaryconsidering t
Page 42 and 43:
Chapter 1IntroductionSummaryIn this
Page 44 and 45:
IntroductionThe combination of memb
Page 46 and 47:
IntroductionThe membranes should ha
Page 48 and 49:
Introductionof water. Energy saving
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number of plants (cum. values)Intro
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IntroductionSubmerged MBR system in
Page 54 and 55:
Introductionchanges of the foulant
Page 56 and 57:
Introductionof 2% NaOH and 0.5% cit
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IntroductionFigure 1.8. Posible rel
Page 60 and 61:
IntroductionSide-stream MBRs involv
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Introductionutilizes the advantages
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Introductionmeans of settlers, of s
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IntroductionUASB, achieving total n
Page 68 and 69:
IntroductionEvenblij, H., van der G
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IntroductionMtinch, E.V., Ban, K.,
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IntroductionYang, S., Yang, F., Fu,
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Chapter 22.1. Liquid phaseIn this s
Page 77 and 78:
Chapter 2where:M fas: molarity of F
Page 79 and 80:
Acetic Acid (mg·L -1 )Chapter 2VFA
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N-NO 2-(mg·L -1 )Chapter 22.1.2.2.
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N-NO 3-(mg·L -1 )Chapter 2interfer
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P-PO 43-(mg·L -1 )Chapter 2Interfe
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Chapter 2alkalinity (IA), which is
Page 89 and 90:
Chapter 22.2.3. Sludge volumetric i
Page 91 and 92:
Chapter 2eq. 2.10eq. 2.11eq. 2.12Th
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Carbohydrate (mg·L -1 )Chapter 2In
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TEP (mgXG·L -1 )Chapter 22.4.4.4.
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Chapter 2Ripley, L.E., Boyle, W.C.,
Page 99 and 100:
Chapter 33.1. IntroductionIn recent
Page 101 and 102:
Chapter 3same in both modules; tap
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Chapter 3phases were varied (table
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Chapter 3to time was higher than 10
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COD removal (%)Chapter 3120100Perio
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DTN and N-NH 4+ (mg·L-1 )DTN and N
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Chapter 3operated with high MLTSS c
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TMP (kPa)TMP (kPa)TMP (kPa)TMP (kPa
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SMP carbohydrates (mg·L -1 )Chapte
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Volume (%)Chapter 3Therefore, the c
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Chapter 3identical to that of the c
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Chapter 3Massé, A. Spérandio, M.,
Page 123 and 124:
Chapter 44.1. IntroductionThe appli
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Chapter 4support were added in this
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Chapter 4This cleaning was performe
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COD (mg·L -1 )COD removal (%)OLR (
Page 131 and 132:
Chapter 4the recirculation ratio be
Page 133 and 134: (mg·L -1 )Chapter 4and ammonium) n
Page 135 and 136: Chapter 4recirculation from the MBR
Page 137 and 138: Chapter 4days 57 (period I) and 316
Page 139 and 140: Chapter 4excellent COD removal perf
Page 141 and 142: Chapter 4Rosenberger, S., Evenblij,
Page 143 and 144: Chapter 55.1. IntroductionAnaerobic
Page 145 and 146: Chapter 55.3. Material and methods5
Page 147 and 148: Chapter 5represented an increment o
Page 149 and 150: Chapter 5operating with similar mem
Page 151 and 152: Chapter 5behaviour might be related
Page 153 and 154: Fouling Rate (Pa·min -1 )Fouling R
Page 155 and 156: Concentration (mg·L -1 )DOC (mg·L
Page 157 and 158: Chapter 5in table 5.3 showed that h
Page 159 and 160: Chapter 5Ho, J., Sung, S. 2010. Met
Page 162 and 163: Chapter 6Denitrification with disso
Page 164 and 165: Denitrification with dissolved meth
Page 174 and 175: (mg·L -1 )Denitrification with dis
Page 176 and 177: DTN effluent (mg·L -1 )CH 4 desorb
Page 186 and 187: Chapter 7Membrane fouling in an AnM
Page 188 and 189: Membrane fouling in an AnMBR treati
Page 194 and 195: OLR and ORR(kgCOD ·m -3·d -1 )pHO
Page 196 and 197: TEP removed (mg·L -1 )OA removed (
Page 198 and 199: R col (m -1 )SRF (m·kg -1 )Membran
Page 200 and 201: BPC, cBPC and TEP concentration(mg
Page 202 and 203: Cake and Colloidal Resistance (m -1
Page 208: Membrane fouling in an AnMBR treati
Page 211 and 212: Conclusionessentido, el uso de una
Page 213 and 214: Conclusionesensuciamiento de la mem
Page 215 and 216: Conclusiónspresenza de soporte de
Page 217 and 218: Conclusións6. Aplicabilidade e per
Page 219 and 220: ConclusionsMoreover, biomass concen
Page 221 and 222: Conclusionstechnology and interesti
Page 223 and 224: List of symbolsHFHRTHyVABHollow Fib
Page 225 and 226: List of symbolsFR/J Normalized Foul
Page 227 and 228: List of publicationsBrand, C., Sán
Page 229: List of publicationsConference on E
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