A new mathematical model to evaluate simazine removal in three different immobilized-biomass reactors

被引:3
作者
Martin, M. [1 ]
Casasus, L. [2 ]
Garbi, C. [1 ]
Nande, M. [1 ]
Vargas, R. [1 ]
Robla, J. I. [3 ]
Sanchez, M. [1 ]
Allende, J. L. [4 ]
机构
[1] Univ Complutense Madrid, Fac Vet, Dept Bioquim & Biol Mol 4, E-28040 Madrid, Spain
[2] Univ Complutense Madrid, Dept Matemat Aplicada, ETSI Ind, Madrid 28006, Spain
[3] CSIC, CENIM, E-28040 Madrid, Spain
[4] Univ Complutense Madrid, Fac Vet, Dept Fis Aplicada, E-28040 Madrid, Spain
关键词
simazine; biomass-reactor; mathematical model; biofilm;
D O I
10.1016/j.watres.2007.09.026
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A new mathematical model based on the cinetical Langmuir equation is developed to interpret and predict the effectiveness of simazine (SZ) removal in immobilized-biomass reactor (IBR), to consider herbicide-support affinity (Cx), and herbicide-cell affinity (Cy). Three solid supports: sepiolite monolith, granular sepiolite, and alginate were used in pilotscale reactors that were inoculated with Klebsiella planticola DSZ. The abiotic process was analysed by measuring the SZ sorption capacity of the reactor supports. Sepiolite monolith showed the maximum value for herbicide- support affinity (28.02 +/- 0.9%). The effectiveness of the biotic process was estimated considering the formation of biomass and SZ biodegradation. Granular sepiolite showed either higher affinity with SZ and viability rate (0.90) throughout the process, and SZ removal rate was 3.39 +/- 0.06 mg/h. The mathematical model presented in this paper provides useful insights into the interpretation of experimental data as well as prediction for the implementation of biological reactors. (c) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1035 / 1042
页数:8
相关论文
共 30 条
[1]   Phase transitions in an elementary probabilistic cellular automaton with memory [J].
Alonso-Sanz, R .
PHYSICA A-STATISTICAL MECHANICS AND ITS APPLICATIONS, 2005, 347 :383-401
[2]  
Alonso-Sanz R, 2006, J CELL AUTOM, V1, P71
[3]  
Alonso-Sanz R, 2005, COMPLEX SYST, V15, P203
[4]   Transient performance of two-phase partitioning bioreactors treating a toluene contaminated gas stream [J].
Boudreau, Neal G. ;
Daugulis, Andrew J. .
BIOTECHNOLOGY AND BIOENGINEERING, 2006, 94 (03) :448-457
[5]   Biofilms:: the matrix revisited [J].
Branda, SS ;
Vik, Å ;
Friedman, L ;
Kolter, R .
TRENDS IN MICROBIOLOGY, 2005, 13 (01) :20-26
[6]   Effects of operating conditions on the adhesive strength of Pseudomonas fluorescens biofilms in tubes [J].
Chen, MJ ;
Zhang, Z ;
Bott, TR .
COLLOIDS AND SURFACES B-BIOINTERFACES, 2005, 43 (02) :61-71
[7]   Modeling physiological resistance in bacterial biofilms [J].
Cogan, NG ;
Cortez, R ;
Fauci, L .
BULLETIN OF MATHEMATICAL BIOLOGY, 2005, 67 (04) :831-853
[8]   MICROBIAL BIOFILMS [J].
COSTERTON, JW ;
LEWANDOWSKI, Z ;
CALDWELL, DE ;
KORBER, DR ;
LAPPINSCOTT, HM .
ANNUAL REVIEW OF MICROBIOLOGY, 1995, 49 :711-745
[9]  
Ferrer E, 1996, PROGR BIOTECHNOL, V11, P762
[10]   Biodegradation of oxadiazon by a soil isolated Pseudomonas fluorescens strain CG5:: Implementation in an herbicide removal reactor and modelling [J].
Garbi, C ;
Casasús, L ;
Martinez-Alvarez, R ;
Robla, JI ;
Martín, M .
WATER RESEARCH, 2006, 40 (06) :1217-1223