Anaerobic treatment of fishery wastewater using a marine sediment inoculum

被引:86
作者
Aspe, E
Marti, MC
Roeckel, M
机构
[1] UNIV CONCEPCION, FAC INGN, DEPT INGN QUIM, CONCEPCION, CHILE
[2] UNIV CONCEPCION, FAC CIENCIAS BIOL, DEPT FARMACOL, CONCEPCION, CHILE
关键词
fish processing effluent; saline substrate; anaerobic treatment; kinetic parameters;
D O I
10.1016/S0043-1354(97)00051-1
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The effluent generated by the Chilean fishmeal industry during hydraulic unloading of fish from ships is high in organic load. After recycling and primary treatment to remove fats and proteins, the effluent contains 4-6 kg COD m(-3) and high salt content (an average of 1.85 kg SO4= m(-3) and 16.2 kg Clm(-3)). Marine sediments and fresh pig manure were assayed as anaerobic inocula to purify this saline effluent. The marine inoculum adapted better and faster at 37 degrees C, Showing a higher final methanogenic/sulphate-reducing bacteria ratio of 0.0025. Specific methanogenic activity at 37 degrees C was 0.065 kg CH4 COD (kg VSS day)(-1), corresponding to 1.3 kg COD (kg VSS)(-1) in 20 days. Methane production was inhibited at COD/SO4= ratios lower than 0.5. A 50% inhibition of the activity was found at 0.22 kg H2S m(-3), 53 kg Na(+)m(-3) and 10 kg SO4= m(-3) respectively; however, at the concentration range in the effluent neither was inhibitory. Kinetic parameters were obtained at 18 and 37 degrees C in mixed flow reactors. At those temperatures, mu(max) values were 0.267 and 0.479 days(-1), while K values for the Chen and Hashimoto model were 2.964 and 1.476, and the growth yield factor (Y) was 0.19 kg VSS (kg COD)(-1). The activation energies were estimated as 3.06 kJ mol(-1) for mu(max) and 27.51 kJ mol(-1) for K. showing that the saline wastewater treatment has a lower temperature dependence than the non-saline one. It was concluded that, under these conditions of high organic load, fishery effluent can be anaerobically treated. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:2147 / 2160
页数:14
相关论文
共 47 条
[1]  
[Anonymous], 2005, STANDARD METHODS EXA, V21
[2]  
APHA, 1985, STAND METH EX WAT WA
[3]  
*ASTM, 1964, IND WAT ATM AN 23
[4]  
BECERRA F, 1990, ALIM EQUIP TECNOL, V4, P147
[5]  
BRYANT MP, 1971, ANAEROBIC BIOL TREAT, V0105, P00023, DOI DOI 10.1021/BA-1971-0105.CH003
[6]   SUBSTRATE UTILIZATION KINETIC-MODEL FOR BIOLOGICAL TREATMENT PROCESSES [J].
CHEN, YR ;
HASHIMOTO, AG .
BIOTECHNOLOGY AND BIOENGINEERING, 1980, 22 (10) :2081-2095
[7]   ANAEROBIC TREATMENT OF SULFATE-CONTAINING WASTE STREAMS [J].
COLLERAN, E ;
FINNEGAN, S ;
LENS, P .
ANTONIE VAN LEEUWENHOEK INTERNATIONAL JOURNAL OF GENERAL AND MOLECULAR MICROBIOLOGY, 1995, 67 (01) :29-46
[8]   KINETICS OF BACTERIAL GROWTH - RELATIONSHIP BETWEEN POPULATION DENSITY AND SPECIFIC GROWTH RATE OF CONTINUOUS CULTURES [J].
CONTOIS, DE .
JOURNAL OF GENERAL MICROBIOLOGY, 1959, 21 (01) :40-50
[9]   SODIUM INHIBITION IN THE ANAEROBIC-DIGESTION PROCESS - ANTAGONISM AND ADAPTATION PHENOMENA [J].
FEIJOO, G ;
SOTO, M ;
MENDEZ, R ;
LEMA, JM .
ENZYME AND MICROBIAL TECHNOLOGY, 1995, 17 (02) :180-188
[10]  
FIELD J, 1995, P INT COURSE ANAEROB, P174