[1]
Runhua Liao, Yan Li, XueMin Yu, et al. Performance and microbial diversity of an expanded granular sludge bed reactor for high sulfate and nitrate waste brine treatment. Journal of Environmental Sciences: Vol. 26(4) (2014), pp.717-725.
DOI: 10.1016/s1001-0742(13)60479-9
Google Scholar
[2]
Runhua Liao, Ke Shen, et al. High-nitrate wastewater treatment in an expanded granular sludge bed reactor and microbial diversity using 454 pyrosequencing analysis. Bioresource Technology: Vol. 134(2013), pp.190-197.
DOI: 10.1016/j.biortech.2012.12.057
Google Scholar
[3]
L. Maharaj, J. Pocock, B.K. Loveday. The effect of distributor configuration on the hydrodynamics of the teetered bed separator. Minerals Engineering: Vol. 20 (11) (2007), pp.1089-1098.
DOI: 10.1016/j.mineng.2007.04.015
Google Scholar
[4]
Jun Wang. Discussion on uniformity of water distribution system of filtration pool. ( In Chinese) Journal of HeFei University of Technology: Vol. 23(6) (2000), pp.1028-1030.
Google Scholar
[5]
Mohammad Asif, Nicolas Kaloge, Leo A. Behie. Hydrodynamics of liquid fluidized beds including the distributor region. Chemical Engineering Science: Vol. 47(15-16) (1992), pp.4155-4166.
DOI: 10.1016/0009-2509(92)85165-8
Google Scholar
[6]
A. Cockx, Z. Do-Quang, J. M. Audic, et al. Global and local mass transfer coefficients in waste water treatment process by computational fluid dynamics. Chem Eng Process: Vol. 40(2) (2001), pp.187-194.
DOI: 10.1016/s0255-2701(00)00138-0
Google Scholar
[7]
K.M. Dhanasekharan, J. Sanyal, A. Jain, et al. A generalized approach to model oxygen transfer in bioreactors using population balances and computational fluid dynamics. Chemical Engineering Science: Vol. 60(1) (2005), pp.213-218.
DOI: 10.1016/j.ces.2004.07.118
Google Scholar
[8]
Xu Wang, Jie Ding, Nan-Qi Ren, Bing-Feng Liu, Wan-Qian Guo. CFD simulation of an expanded granular sludge bed (EGSB) reactor for biohydrogen production. International Journal of Hydrogen Energy: Vol. 34(24) (2009), pp.9685-9695.
DOI: 10.1016/j.ijhydene.2009.10.027
Google Scholar
[9]
Xu Wang, Jie Ding, Wan-Qian Guo, Nan-Qi Ren. A Hydrodynamics-Reaction kinetics coupled model for evaluating bioreactors derived from CFD simulation. Bioresource Technology: Vol. 101(2010), pp.9749-9757.
DOI: 10.1016/j.biortech.2010.07.115
Google Scholar
[10]
Feng Qian, Xue Zhao-xia and Wang Hui. Application of CFD theory in optimal design and operation of water treatment reactor. (In Chinese) Water Resources Protection: Vol. 22(2) (2006), pp.11-15.
Google Scholar
[11]
L. Diez, B.E. Zima, W. Kowalczyk, et al. Investigation of multiphase flow in sequencing batch reactor (SBR) by means of hybrid methods. Chemical Engineering Science: Vol. 62(2) (2007), pp.1803-1813.
DOI: 10.1016/j.ces.2006.12.005
Google Scholar
[12]
He J.G., et al. Analysis of mass transfer in mixing process and introduction of a new evaluation factor named mixing factor. (In Chinese) Journal of Harbin Institute of Technology: Vol. 40(12) (2008), p.1937-(1940).
Google Scholar
[13]
Jiang X., Chen G. t., Li X. Particle/ Fluid mass transfer in turbulence. (In Chinese) Journal of Chemical Engineering of Chinese Universities: Vol. 03(1996), pp.37-42.
Google Scholar
[14]
Kwok W K. Influence of biomass production and detachment forces on biofilm structures in a biofilm airlift suspension reactor. Biotechnol. Bioeng: Vol. 58(1998), pp.400-407.
DOI: 10.1002/(sici)1097-0290(19980520)58:4<400::aid-bit7>3.0.co;2-n
Google Scholar
[15]
Yongqiang L, Yu L and Tay J.H. Appl. The effects of extracellular polymeric substances on the formation and stability of biogranules. (In Chinese) Microbiol. Biotechnol: Vol. 65(2004), pp.143-148.
DOI: 10.1007/s00253-004-1657-8
Google Scholar