Combining submerged membrane technology with anaerobic and ...

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number of plants (cum. values)IntroductionIn Europe and Asia more research in the area of urban wastewater treatment than inindustrial was carried out while in Northamerica the situation was reversed, because inEurope and Asia there was more space restrictions to expand conventional treatmentplants, making membrane technology very attractive for the treatment of wastewater withhigh flow and low organic loads, such as urban (Lesjean et al., 2004).1.3.2. MarketOver the past twenty years, research has been focused mainly to determine thefeasibility of MBR technology, and the search for methods to improve the process. As aresult, MBRs are increasingly becoming the technology of choice for water and wastewaterapplications where the above criteria apply, as is evident by the substantial increase in themembrane bioreactor market over recent years - MBRs are now implemented in more than200 countries and global market growth rates of between 11.5% and 13% are regularlyreported in market analysis reports, the MBR industry market value being estimated asworth $500 million by 2013 (Judd, 2011).In figure 1.6 can be observed the evolution of the MBR implementation in Europeduring the last two decades for the treatment of both industrial and municipal wastewaters.Although some industrial applications were the first niche for MBR technology, theprogressive reduction of operational costs has made this technology competitive formunicipal wastewater treatment during the last decade.600500400Industrial (capacity>20m3/d)Municipal (capacity>100 m3/d)3002001000YearFigure 1.6. Number of MBR in Europe (Huisjes et al., 2009).37
Chapter 1Table 1.2. Main suppliers of submerged MBR technology (adapted from Santos et al.,2010 and www.thembrsite.com).FS Supplier Country HF Supplier CountryA3 Germany Asahi Kasei JapanAlfa Laval Sweden Beijing Origin Water China/TaiwanAnua USA Canpure CanadaBrightwater S. Ireland Ecologix China/TaiwanColloide N. Ireland ECONITY KoreaEcologix Canada ENE KoreaHuber Germany GE Zenon USAHyflux Singapore Hainan Litree China/TaiwanLG Korea Hangzhou H-Filtration China/TaiwanKubota Japan Koch Memb. Syst (PURON) USAMartin Systems Germany Memstar SingaporeMicrodyn-Nadir Germany Micronet Porous Fibers SpainPure Envitech Korea Mitsubishi Rayon JapanShanghai Megavision China/Taiwan Philos KoreaShangai SINAP China/Taiwan SENUO FiltrationChina/TaiwanSuzhou Vina China/TaiwanTechnologyShanghai Dehong China/TaiwanToray Japan Siemens GermanyWeise Germany Sumitono JapanSuperstringSuzhou VinaTianjin MotimoZena SROChina/TaiwanChina/TaiwanChina/TaiwanCzech Rep.38
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Page 6 and 7: padres Macario y Marisa, les agrade
Page 8 and 9: 2.1.2. Nitrogen compounds 662.1.2.1
Page 10: 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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Page 34 and 35: Objectives and summaryThis thesis i
Page 36 and 37: Objectives and summaryOn the basis
Page 38 and 39: Objectives and summaryfrom the MBR
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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
Page 52 and 53: IntroductionSubmerged MBR system in
Page 54 and 55: Introductionchanges of the foulant
Page 56 and 57: Introductionof 2% NaOH and 0.5% cit
Page 58 and 59: IntroductionFigure 1.8. Posible rel
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Page 62 and 63: Introductionutilizes the advantages
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Page 66 and 67: IntroductionUASB, achieving total n
Page 68 and 69: IntroductionEvenblij, H., van der G
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Page 72: IntroductionYang, S., Yang, F., Fu,
Page 75 and 76: 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
Page 81 and 82: N-NO 2-(mg·L -1 )Chapter 22.1.2.2.
Page 83 and 84: N-NO 3-(mg·L -1 )Chapter 2interfer
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Page 87 and 88: 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
Page 93 and 94: Carbohydrate (mg·L -1 )Chapter 2In
Page 95 and 96: TEP (mgXG·L -1 )Chapter 22.4.4.4.
Page 97 and 98: Chapter 2Ripley, L.E., Boyle, W.C.,
Page 99 and 100: Chapter 33.1. IntroductionIn recent
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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.,
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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 (
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Chapter 4the recirculation ratio be
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(mg·L -1 )Chapter 4and ammonium) n
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Chapter 4recirculation from the MBR
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Chapter 4days 57 (period I) and 316
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Chapter 4excellent COD removal perf
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Chapter 4Rosenberger, S., Evenblij,
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Chapter 55.1. IntroductionAnaerobic
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Chapter 55.3. Material and methods5
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Chapter 5represented an increment o
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Chapter 5operating with similar mem
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Chapter 5behaviour might be related
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Fouling Rate (Pa·min -1 )Fouling R
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Concentration (mg·L -1 )DOC (mg·L
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Chapter 5in table 5.3 showed that h
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Chapter 5Ho, J., Sung, S. 2010. Met
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Chapter 6Denitrification with disso
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Denitrification with dissolved meth
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(mg·L -1 )Denitrification with dis
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DTN effluent (mg·L -1 )CH 4 desorb
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Chapter 7Membrane fouling in an AnM
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Membrane fouling in an AnMBR treati
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OLR and ORR(kgCOD ·m -3·d -1 )pHO
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TEP removed (mg·L -1 )OA removed (
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R col (m -1 )SRF (m·kg -1 )Membran
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BPC, cBPC and TEP concentration(mg
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Cake and Colloidal Resistance (m -1
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Conclusionessentido, el uso de una
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Conclusionesensuciamiento de la mem
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Conclusiónspresenza de soporte de
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Conclusións6. Aplicabilidade e per
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ConclusionsMoreover, biomass concen
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Conclusionstechnology and interesti
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List of symbolsHFHRTHyVABHollow Fib
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List of symbolsFR/J Normalized Foul
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List of publicationsBrand, C., Sán
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List of publicationsConference on E
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