User-Friendly Mathematical Model for the Design of Sulfate Reducing H2/CO2 Fed Bioreactors

被引:10
作者
Esposito, G. [1 ]
Lens, P. [2 ]
Pirozzi, F. [3 ]
机构
[1] Univ Cassino, Dept Mech Struct & Environm Engn, I-03043 Cassino, FR, Italy
[2] UNESCO, IHE, NL-2601 DA Delft, Netherlands
[3] Univ Naples Federico 2, Dept Hydraul Geotechn & Environm Engn, I-80125 Naples, Italy
来源
JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE | 2009年 / 135卷 / 03期
关键词
GAS-LIFT REACTOR; METHANOGENIC BACTERIA; LOW-TEMPERATURE; COMPETITION; REDUCTION; REDUCERS; HYDROGEN; KINETICS; GROWTH; SYSTEM;
D O I
10.1061/(ASCE)0733-9372(2009)135:3(167)
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This paper presents three steady-state mathematical models for the design of H-2/CO2 fed gas-lift reactors aimed at biological sulfate reduction to remove sulfate from wastewater. Models 1A and 1B are based on heterotrophic sulfate reducing bacteria (HSRB), while Model 2 is based on autotrophic sulfate reducing bacteria (ASRB) as the dominant group of sulfate reducers in the gas-lift reactor. Once the influent wastewater characteristics are known and the desired sulfate removal efficiency is fixed, all models give explicit mathematical relationships to determine the bioreactor volume and the effluent concentrations of substrates and products. The derived explicit relationships make application of the models very easy, fast, and no iterative procedures are required. Model simulations show that the size of the H-2/CO2 fed gas-lift reactors aimed at biological sulfate removal from wastewater highly depends on the number and type of trophic groups growing in the bioreactor. In particular, if the biological sulfate reduction is performed in a bioreactor where ASRB prevail, the required bioreactor volume is much smaller than that needed with HSRB. This is because ASRB can out-compete methanogenic archaea (MA) for H-2 (assuming sulfate concentrations are not limiting), whereas HSRB do not necessarily out-compete MA due to their dependence on homoacetogenic bacteria (HB) for organic carbon. The reactor sizes to reach the same sulfate removal efficiency by HSRB and ASRB are only comparable when methanogenesis is inhibited. Moreover, model results indicate that acetate supply to the reactor influent does not affect the HSRB biomass required in the reactor, but favors the dominance of MA on HB as a consequence of a lower HB requirement for acetate supply.
引用
收藏
页码:167 / 175
页数:9
相关论文
共 28 条
[1]   A STEADY-STATE MODEL FOR THE SINGLE SLUDGE ACTIVATED-SLUDGE SYSTEM .1. MODEL DESCRIPTION [J].
ARGAMAN, Y .
WATER RESEARCH, 1995, 29 (01) :137-145
[2]   LITHOAUTOTROPHIC GROWTH OF SULFATE-REDUCING BACTERIA, AND DESCRIPTION OF DESULFOBACTERIUM-AUTOTROPHICUM GEN-NOV, SP-NOV [J].
BRYSCH, K ;
SCHNEIDER, C ;
FUCHS, G ;
WIDDEL, F .
ARCHIVES OF MICROBIOLOGY, 1987, 148 (04) :264-274
[3]  
Elferink S.J. W. H. Oude., 1994, FEMS Microbiol. Rev, V15, P119, DOI DOI 10.1111/j.1574-6976.1994.tb00130.x
[4]   Effect of the sludge retention time on H2 utilization in a sulphate reducing gas-lift reactor [J].
Esposito, G ;
Weijma, J ;
Pirozzi, F ;
Lens, PNL .
PROCESS BIOCHEMISTRY, 2003, 39 (04) :491-498
[5]   Four-substrate design model for single sludge predenitrification system [J].
Esposito, G ;
Fabbricino, M ;
Pirozzi, F .
JOURNAL OF ENVIRONMENTAL ENGINEERING, 2003, 129 (05) :394-401
[6]   Extension of Anaerobic Digestion Model No. 1 with processes of sulfate reduction [J].
Fedorovich, V ;
Lens, P ;
Kalyuzhnyi, S .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2003, 109 (1-3) :33-45
[7]   METHANOGENESIS AND SULFATE REDUCTION IN CHEMOSTATS .2. MODEL DEVELOPMENT AND VERIFICATION [J].
GUPTA, A ;
FLORA, JRV ;
SAYLES, GD ;
SUIDAN, MT .
WATER RESEARCH, 1994, 28 (04) :795-803
[8]  
Henze M., 2000, ACTIVATED SLUDGE MOD, DOI DOI 10.2166/9781780402369
[9]  
Herrera L, 1997, ENVIRON TOXIC WATER, V12, P101, DOI 10.1002/(SICI)1098-2256(1997)12:2<101::AID-TOX1>3.0.CO
[10]  
2-C