Influence of the tracer characteristics on hydrodynamic models of packed-bed bioreactors

被引:45
作者
de Nardi, IR [1 ]
Zaiat, M [1 ]
Foresti, E [1 ]
机构
[1] Univ Sao Paulo, Escola Engn Sao Carlos, CEP, BR-13560250 Sao Carlos, SP, Brazil
基金
巴西圣保罗研究基金会;
关键词
Porous Medium; Residence Time Distribution; Tracer Diffusion; Bromocresol; Hydraulic Residence Time;
D O I
10.1007/s004490050704
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
A bench-scale horizontal-flow anaerobic immobilized sludge (HAIS) reactor filled with porous ceramic spheres (5 mm diameter) was used for evaluating the effects of the tracer characteristics on the residence time distribution (RTD) curves and on the parameters of the hydrodynamic mathematical models. Stimulus-response assays were carried out with bromophenol blue, a dextran blue, eosin Y, mordant violet, rhodamine WT and bromocresol green as tracers. The reactor was operated at the hydraulic residence time (HRT) of approximately 2 hours and the flow characteristics were evaluated by fitting the single-parameter models of dispersion and N-continuous stirred tank reactors (CSTR) in series to the experimental data. Tracer characteristics were found to affect deeply the form of RTD curves and the apparent degree of mixing observed in the responses were attributed to the tracer diffusion into the porous media, except for dextran blue. The best adjustment was obtained for the N-CSTR in series model. Thereafter, dextran blue and rhodamine WT were used in hydrodynamic experiments in the HAIS reactor operating with additional residence times. Values of N ranging from 34 to 62 were obtained from the dextran blue experiments for HRT ranging from 2 to 7 hours. The application of the statistical analysis ANOVA one-way method indicated that there was no significant statistical difference in the flow-pattern within the range of hydraulic residence times applied. The mean N value of 9 was obtained from the experiments with rhodamine WT. Such disagreement in the responses was attributed to the diffusion of rhodamine WT into the porous media, interfering in the shape of the experimental curves.
引用
收藏
页码:469 / 476
页数:8
相关论文
共 11 条
[1]  
CABRAL AKA, 1995, THESIS EESC USP SAO
[2]  
Foresti E., 1995, BRAZ J CHEM ENG, V12, P235
[3]  
JIMENEZ B, 1988, Biotechnology Techniques, V2, P77, DOI 10.1007/BF01876154
[4]   DEXTRAN BLUE COLORANT AS A RELIABLE TRACER IN SUBMERGED FILTERS [J].
JIMENEZ, B ;
NOYOLA, A ;
CAPDEVILLE, B ;
ROUSTAN, M ;
FAUP, G .
WATER RESEARCH, 1988, 22 (10) :1253-1257
[5]  
Levenspiel O, 1972, CHEM REACTORS ENG
[6]  
Neter J., 1990, APPL STAT MODELS
[7]  
Smith J.M., 1981, CHEM ENG KINETICS, VThird
[8]  
Speece R.E., 1996, Anaerobic Biotechnology and Odor/Corrosion Control for Municipalities and Industries
[9]   LIQUID RESIDENCE TIME DISTRIBUTIONS IN IMMOBILIZED CELL BIOREACTORS [J].
SWAINE, DE ;
DAUGULIS, AJ .
BIOTECHNOLOGY AND BIOENGINEERING, 1989, 33 (05) :604-612
[10]  
Zaiat M, 1997, BIOTECHNOL BIOENG, V53, P220, DOI 10.1002/(SICI)1097-0290(19970120)53:2<220::AID-BIT13>3.0.CO