UTILIZATION OF VOLATILE FATTY-ACIDS IN METHANOGENIC BIOFILMS

被引:12
作者
YU, J [1 ]
PINDER, KL [1 ]
机构
[1] DEPT CHEM ENGN, VANCOUVER V6T 1Z4, BC, CANADA
关键词
VOLATILE FATTY ACIDS; ANAEROBIC METHANATION; BIOFILM; KINETICS; MASS TRANSFER RESISTANCE;
D O I
10.1016/0960-8524(93)90127-W
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Utilization kinetics of volatile fatty acids (acetic, propionic and butyric acids) in mesophilic (35-degrees-C) methane-producing biofilms were investigated in a continuous flow reactor. The mass transfer resistances occurring inside and outside biofilms were tested and minimized during the experiments. By monitoring the biofilm growth in terms of carbon content (mgC), the utilization rate of each fatty acid was measured per unit biomass of a balanced symbiotic biofilm containing all concerned bacterial groups. The experiments were designed and conducted to avoid bacterial population shift in the mixed consortium. Thereby, the relations between utilization rates and concentrations of the volatile fatty acids were governed and explained by enzyme-catalyzed substrate catabolisms. The acetate utilization rate fits a Monod model quite well while consumption rates of propionic and butyric acids deviated from the two-parameter model to some degree. It was found that high propionate concentrations promoted propionate utilization but inhibited butyrate consumption. Three-parameter models were discussed to fit the experimental data better. Judged by the Monod model parameters, acetate was utilized at the fastest rate with a maximum rate of 0.098 mg HAc mg C-1 h-1 followed by butyrate (apparent maximum utilization rate of 0.0334 mg HBu mg C-1 h-1) and propionate (apparent maximum utilization rate of 0.021 mg HPr mg C-1 h-1). Butyrate utilization had the lowest apparent half velocity concentration (20 mg HBu liter-1) followed by propionate utilization (99 mg HPr liter-1) while acetate utilization had the highest half velocity concentration (160 mg HAc liter-1).
引用
收藏
页码:241 / 250
页数:10
相关论文
共 32 条
[1]  
BAJPAJ AC, 1977, ADV ENG MATH, P110
[2]  
Dolfing J., 1988, BIOL ANAEROBIC MICRO, P417
[3]  
EASTMAN JA, 1981, J WATER POLLUT CON F, V53, P352
[4]   INFLUENCE OF HIGH SUBSTRATE CONCENTRATIONS ON MICROBIAL KINETICS [J].
EDWARDS, VH .
BIOTECHNOLOGY AND BIOENGINEERING, 1970, 12 (05) :679-+
[5]   METHANE PRODUCTION FROM INDUSTRIAL-WASTES BY 2-PHASE ANAEROBIC-DIGESTION [J].
GHOSH, S ;
OMBREGT, JP ;
PIPYN, P .
WATER RESEARCH, 1985, 19 (09) :1083-1088
[6]   INFLUENCE OF MASS-TRANSFER LIMITATIONS ON DETERMINATION OF THE HALF SATURATION CONSTANT FOR HYDROGEN UPTAKE IN A MIXED-CULTURE CH4-PRODUCING ENRICHMENT [J].
GIRALDOGOMEZ, E ;
GOODWIN, S ;
SWITZENBAUM, MS .
BIOTECHNOLOGY AND BIOENGINEERING, 1992, 40 (07) :768-776
[7]   2-STAGE ANAEROBIC-DIGESTION FOR THE TREATMENT OF CELLULOSIC WASTES [J].
GIRARD, P ;
SCHARER, JM ;
MOOYOUNG, M .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1986, 33 (01) :B1-B10
[8]   CONVERSION PROCESSES IN ANAEROBIC-DIGESTION [J].
GUJER, W ;
ZEHNDER, AJB .
WATER SCIENCE AND TECHNOLOGY, 1983, 15 (8-9) :127-167
[9]  
HENZE M, 1983, WATER SCI TECHNOL, V15, P1
[10]   LONG-CHAIN VOLATILE FATTY-ACID RELATIONSHIPS IN ANAEROBIC-DIGESTION OF SWINE WASTE [J].
HILL, DT ;
HOLMBERG, RD .
BIOLOGICAL WASTES, 1988, 23 (03) :195-214