Feasibility of methanolic waste treatment in UASB reactors

被引:28
作者
Bhatti, ZI [1 ]
Furukawa, K [1 ]
Fujita, M [1 ]
机构
[1] OSAKA UNIV,FAC ENGN,DEPT ENVIRONM ENGN,SUITA,OSAKA 565,JAPAN
关键词
UASB reactor; methanolic waste treatment; feasibility; pH; HRT; methanogens;
D O I
10.1016/S0043-1354(96)00144-3
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Feasibility of methanolic waste treatment in an upflow anaerobic sludge blanket (UASB) reactor operating continuously for a period of more than 400 days was examined. Optimum pH was found to be between 7.0-7.3. In this pH range, there was no excessive build-up of volatile fatty acids and no upset or reactor failure was observed. Elementary pathways of degradation of methanol to methane were shown to be governed by the operating pH. Permissible volumetric loading rate to achieve 80% of TOC removal efficiency was determined to be 8 g-TOC/1 . d. Below this value, the effect of hydraulic retention time or loading rate on TOC removal efficiency was not pronounced. Kinetic coefficients of k, Ks, Y and b were determined to be 1.11g-TOC/g-VSS . d, 0.385g-TOC/1, 0.213g-VSS/g-TOC and 0.005 d(-1), respectively. Maximum specific methanogenic activity was experimentally found to be 2 g-CH4-COD/g-VSS . d while maximum specific loading rate to achieve 80% of TOC removal efficiency was determined to be 2 g-TOC/g-VSS . d. The results of this study suggest that single-step anaerobic treatment of methanolic waste is highly feasible provided that the PH is maintained close to 7.0. Copyright (C) 1996 Elsevier Science Ltd
引用
收藏
页码:2559 / 2568
页数:10
相关论文
共 32 条
[1]  
ALPHENAAR PA, 1993, APPL MICROBIOL BIOT, V39, P276, DOI 10.1007/BF00228619
[2]  
Andrews J, 1969, J SANIT ENG DIV ASCE, V1, P95
[3]  
[Anonymous], STAND METH EX WAT WA
[4]   TREATMENT PERFORMANCE AND MICROBIAL STRUCTURE OF A GRANULAR CONSORTIUM HANDLING METHANOLIC WASTE [J].
BHATTI, ZI ;
FURUKAWA, K ;
FUJITA, M .
JOURNAL OF FERMENTATION AND BIOENGINEERING, 1993, 76 (03) :218-223
[5]  
BHATTI ZI, 1995, 3 INT C APPR WAST MA
[6]  
BHATTI ZI, 1993, JAP J WAT TREAT BIOL, V29, P51
[7]   STRUCTURED MODELING OF THE ANAEROBIC-DIGESTION OF BIOMASS PARTICULATES [J].
BRYERS, JD .
BIOTECHNOLOGY AND BIOENGINEERING, 1985, 27 (05) :638-649
[8]   ANAEROBIC-DIGESTION OF WOOD ETHANOL STILLAGE USING UPFLOW ANAEROBIC SLUDGE BLANKET REACTOR [J].
CALLANDER, IJ ;
CLARK, TA ;
MCFARLANE, PN .
BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (07) :896-908
[9]  
CHRISTENSEN DR, 1984, J WATER POLLUT CON F, V56, P1059
[10]  
DENAC M, 1986, BIOTECHNOL BIOENG, V31, P1