PAI T Y,TSAI Y P,CHOU Y J,et al.Microbial kinetic analysis of three different types of EBNR process[J].Chemosphere,2004,55(1):109-118.
[2]
ZHU G B,PENG Y Z,ZHAI L M,et al.Performance and optimization of biological nitrogen removal process enhanced byanoxic/oxic step feeding[J].Biochemical Engineering Journal,2009,43(3):280-287.
[3]
ZHU G B,PENG Y Z,MA B,et al.Optimization of anoxic/oxic step feeding active sludge process with fuzzy control modelfor improving nitrogen removal[J].Chemical Engineering Journal,2009,151(1/3):195-201.
[4]
BARLINDHAUG J,ODEGARD H.Thermal hydrolysate as a carbon source for denitrification[J].Water Science andTechnology,1996,33(12):99-108.
[5]
ZAYED G,WINTER J.Removal of organic pollutants and nitrate from wastewater from the dairy industry by denitrification[J].Applied Microbiology and Biotechnology,1998,49(4):469-474.
[6]
SAGE M,DAUFIN G,GSAN-GUIZIOU G,et al.Denitrification potential and rates of complex carbon source from dairyeffluents in activated sludge system[J].Water Research,2006,40(14):2747-2755.
[7]
KUJAWA K,KLAPWIJK B.A method to estimate denitrification potential for pre-denitrification systems using NUR batchtests[J].Water Research,1999,33(10):2291-2300.
[8]
NYBERG U,ASPEGREN H,ANDERSSON B,et al.Full-scale applications of nitrogen removal with methanol as carbonsource[J].Water Science and Technology,1992,26(5/6):1077-1086.
[9]
TAM N F Y,WONG Y S,LEUNG G.Significance of external carbon sources on simultaneous removal of nutrients fromwastewater[J].Water Science and Technology,1992,26(1/2):104721055.
[10]
GERBER A,MOSTERT E S,WINTER C T,et al.The effect of acetate and other short-chain carbon compounds on thekinetics of biological nutrient removal[J].Water SA,1986,12(20):7-12.
[11]
HENZE M,GRADY C J,GUJER W,et al.Activated sludge model No.1.IAWPRC scientific and Technical Report No.1[M].London:IAWPRC,1987.
[12]
HENZE M,GUJER W,MINO T,et al.Activated sludge model No.2.IAWQ scientific and Technical Report No.3[M].London:IAWPRC,1987.
[13]
KRISTENSEN G H,JORGENSEN P T.Precipitation followed by biological denitrification supported by addition of biologicalor thermal/chemical hydrolysis products[C]∥Proceedings from 4th Gothenburg Symposium.Madrid:Springer Verlag,1990:313-328.
[14]
ELEFSINIOTIS P,LI D.The effect of temperature and carbon source on denitrification using volatile fatty acids[J].Biochemical Engineering Journal,2006,28(1):148-155.
[15]
BEAUBIEN A,HU Y,BELLAHCEN D,et al.Denitrification processes using gas production measurements[J].WaterResearch,1995,29(10):2269-2274.
[16]
HENZE M,HARREMOES P.Chemical biological nutrient removal:the HYPRO concept[C]∥Proceedings of the 4thGothenburg Symposium Chemical Water and Wastewater Treatment.Madrid:Springer Verlag,1990:145-149.
[17]
HENZE M.Nitrate versus oxygen utilization rates in wastewater and activated sludge systems[J].Water Science andTechnology,1986,18(6):115-122.
[18]
HENZE M.The influence of raw wastewater biomass on activated sludge oxygen respiration rates and denitrification rates[J].Water Science and Technology,1989,21(6/7):603-607.
[19]
HENZE M.Capabilities of biological nitrogen removal processes from wastewater[J].Water Science and Technology,1991,23(4/6):669-679.
[20]
LOUZEIRO N R,MAVINIC D S,OLDHAM WK,et al.Methanol induced biological nutrient removal kinetics in a full scalesequencing batch reactor[J].Water Research,2002,36(11):2721-2732.
[21]
LEE N,WELANDER T.The effect of different carbon sources on respiratory denitrification in biological wastewater treatment[J].Journal of Biotechnology and Bioengineering,1996,82(3):277-285.
[22]
MULLER A,WENTZEL M C,LOEWENTHAL R E,et al.Heterotroph anoxic yield in anoxic aerobic activated sludgesystem treating municipal wastewater[J].Water Research,2003,37(10):2435-2441.
[23]
BEUN J J,VERHOEF E V,VAN LOOSDRECHT M C M,et al.Stoichiometry and kinetics of poly-β-hydroxybutyratemetabolism under denitrifying conditions in activated sludge cultures[J].Biotechnology and Bioengineering,2000,68(5):496-507.