Two-phase, two-stage, and single-stage anaerobic process comparison

被引:43
作者
Azbar, N [1 ]
Speece, RE
机构
[1] Balikesir Univ, Dept Environm Engn, TR-10100 Balikesir, Turkey
[2] Vanderbilt Univ, Dept Civil & Environm Engn, Nashville, TN 37235 USA
基金
新加坡国家研究基金会;
关键词
D O I
10.1061/(ASCE)0733-9372(2001)127:3(240)
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In this research, three anaerobic process configurations-namely, two-phase dual sludge (TPDS), two-stage single sludge (TSSS), and single-stage-were evaluated for effluent COD concentration. The same temperature, SRT, and glucose substrate were used in all experiments. In every case, TPDS and TSSS configurations significantly outperformed the single stage. All experiments were carried out at a temperature of 35 degreesC, end all reactors were operated as daily fill-and-draw with HRT = SRT. The following ranges for each design parameter were studied: pH (4.5, 5.5, and 6.5); first stage HRT (3, 8, and 24 h); and flee load (3, 9, and 27 gCOD/gVSS). The overall HRT/SRT of all systems was 30 days, and a pH-Stat system was used to control the pH in the acidification reactors at the desired value. Statistical evaluation of the results indicated that a flee load of 3 in the first reactor of TPDS yielded the lowest effluent COD concentrations under the studied range of parameters, while fur the TSSS reactor configuration the staging of the system itself was the controlling phenomena responsible for reduced effluent GOD.
引用
收藏
页码:240 / 248
页数:9
相关论文
共 35 条
[1]   MICROBIOLOGICAL STUDY OF 2-STAGE ANAEROBIC-DIGESTION DURING START-UP [J].
ANDERSON, GK ;
KASAPGIL, B ;
INCE, O .
WATER RESEARCH, 1994, 28 (11) :2383-2392
[2]  
[Anonymous], 1992, STAND METH EX WAT WA
[3]   STEADY-STATE AND TRANSIENT-BEHAVIOR IN MICROBIAL METHANIFICATION .1. EXPERIMENTAL RESULTS [J].
BHATIA, D ;
VIETH, WR ;
VENKATASUBRAMANIAN, K .
BIOTECHNOLOGY AND BIOENGINEERING, 1985, 27 (08) :1192-1198
[4]   HYDROLYSIS AND ACIDOGENIC FERMENTATION OF A PROTEIN, GELATIN, IN AN ANAEROBIC CONTINUOUS CULTURE [J].
BREURE, AM ;
VANANDEL, JG .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1984, 20 (01) :40-45
[5]   AN EVALUATION OF SINGLE-PHASE AND SEPARATED-PHASE ANAEROBIC INDUSTRIAL WASTEWATER-TREATMENT IN FLUIDIZED-BED REACTORS [J].
BULL, MA ;
STERRITT, RM ;
LESTER, JN .
BIOTECHNOLOGY AND BIOENGINEERING, 1984, 26 (09) :1054-1065
[6]   ANAEROBIC DIGESTION OF GLUCOSE WITH SEPARATED ACID PRODUCTION AND METHANE FORMATION [J].
COHEN, A ;
ZOETEMEYER, RJ ;
VANDEURSEN, A ;
VANANDEL, JG .
WATER RESEARCH, 1979, 13 (07) :571-580
[7]   INFLUENCE OF PHASE-SEPARATION ON THE ANAEROBIC-DIGESTION OF GLUCOSE .1. MAXIMUM COD TURNOVER RATE DURING CONTINUOUS OPERATION [J].
COHEN, A ;
BREURE, AM ;
VANANDEL, JG ;
VANDEURSEN, A .
WATER RESEARCH, 1980, 14 (10) :1439-1448
[8]   CHARACTERIZATION OF ANAEROBIC MICROBIAL CULTURE WITH HIGH ACIDOGENIC ACTIVITY [J].
DELATORRE, I ;
GOMA, G .
BIOTECHNOLOGY AND BIOENGINEERING, 1981, 23 (01) :185-199
[9]  
DEMIRER G, 1996, THESIS VANDERBILT U
[10]   ANAEROBIC ACIDOGENESIS OF A COMPLEX WASTE-WATER .1. THE INFLUENCE OF OPERATIONAL PARAMETERS ON REACTOR PERFORMANCE [J].
DINOPOULOU, G ;
RUDD, T ;
LESTER, JN .
BIOTECHNOLOGY AND BIOENGINEERING, 1988, 31 (09) :958-968