TREATMENT OF SEAFOOD-PROCESSING WASTEWATERS IN MESOPHILIC AND THERMOPHILIC ANAEROBIC FILTERS

被引:67
作者
MENDEZ, R [1 ]
LEMA, JM [1 ]
SOTO, M [1 ]
机构
[1] UNIV A CORUNA,DEPT FUNDAMENTAL & IND CHEM,CORUNA,SPAIN
关键词
ANAEROBIC; FILTER; SALINITY; SEAFOOD WASTES; TEMPERATURE;
D O I
10.2175/106143095X131178
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Wastewaters from fish-canning industries have a high concentration of organic polluting substances (10-50 g chemical oxygen demand L-1 [COD]) and, in some cases, a high content of sea salts (Cl-: 8-19 g L-1, Na+:5-12 g L-1, SO4(2-): 0.6-2.7 g L-1). The presence of high sodium ion concentration in wastewaters with high organic content traditionally is considered as a very negative factor for their anaerobic treatment. In fact, both the presence of Na+ and SO4(2-), transformed into H2S during the anaerobic degradation process, may caus toxicity and inhibition on the methanogenic process. This work deals with the operation and treatment efficiency of two lab-scale mesophilic and thermophilic anaerobic filters (MAF and TAF, respectively). So that the adaptation of anaerobic sludge to high saline concentrations is attained, a prolonged start-up period of about nine months was necessary. After this, a stable operation and similar treatment efficiencies were reached, even when organic loading rate (OLR) as high as 9 kg COD m-3 d-1 (TAF) or 24 kg COD m-3 d-1 (MAF) were applied at chloride concentration of 13 g L-1. At these conditions, the COD removal reached 73% (TAF) and 64% (MAF), and the COD methanized reached 69% (TAF) and 66% (MAF). The sulphate in the influent was removed practically completely, leading to a H2S concentration in the biogas between 3-4%. In spite of the lower specific activity of sludge from MAF (0.21 g COD g-1 volatile suspended solids [VSS] d-1) than from TAF (0.66), the MAF reached a higher OLR than TAF. This fact can be explained because of the higher retention of sludge into MAF (72 g VSS L-1) than TAF (10 g VSS L-1). Two practical conclusions may be derived from this work: the thermophilic operation needs the use of a packing material with a higher capacity to retain biomass and the mesophilic operation requires a more frequent detachment of biomass from the support in order to avoid clogging problems.
引用
收藏
页码:33 / 45
页数:13
相关论文
共 32 条
[1]   LIQUID EFFLUENTS OF THE FISH CANNING INDUSTRIES OF RIO DE JANEIRO STATE - TREATMENT ALTERNATIVES [J].
AGUIAR, ALC ;
SANTANNA, GL .
ENVIRONMENTAL TECHNOLOGY LETTERS, 1988, 9 (05) :421-428
[2]  
AHRING BK, 1991, APPL MICROBIOL BIOT, V35, P686
[3]  
[Anonymous], 1985, STANDARD METHODS EXA
[4]   PILOT-SCALE EXPERIMENTS ON ANAEROBIC TREATMENT OF WASTE-WATER FROM A FISH PROCESSING PLANT [J].
BALSLEVOLESEN, P ;
LYNGGAARDJENSEN, A ;
NICKELSEN, C .
WATER SCIENCE AND TECHNOLOGY, 1990, 22 (1-2) :463-474
[5]  
CAROZZI A, 1988, 5TH P INT S AN DIG B, P547
[6]  
CHUNG YC, 1988, J WATER POLLUT CON F, V60, P107
[7]   ACTIVITY MEASUREMENTS AS A TOOL TO CHARACTERIZE THE MICROBIAL COMPOSITION OF METHANOGENIC ENVIRONMENTS [J].
DOLFING, J ;
BLOEMEN, WGBM .
JOURNAL OF MICROBIOLOGICAL METHODS, 1985, 4 (01) :1-12
[8]  
GUERRERO L, 1992, THESIS U SANTIAGO CO
[9]   RECENT DEVELOPMENTS IN HYDROGEN MANAGEMENT DURING ANAEROBIC BIOLOGICAL WASTE-WATER TREATMENT [J].
HARPER, SR ;
POHLAND, FG .
BIOTECHNOLOGY AND BIOENGINEERING, 1986, 28 (04) :585-602
[10]   ANAEROBIC-DIGESTION OF A SULFATE-RICH MOLASSES WASTE-WATER - INHIBITION OF HYDROGEN-SULFIDE PRODUCTION [J].
HILTON, MG ;
ARCHER, DB .
BIOTECHNOLOGY AND BIOENGINEERING, 1988, 31 (08) :885-888