Continuous anaerobic treatment of wastewaters containing formaldehyde and urea

被引:41
作者
Vidal, G
Jiang, ZP
Omil, F
Thalasso, F
Méndez, R
Lema, JM
机构
[1] Univ Santiago de Compostela, Dept Chem Engn, E-15706 Santiago, Spain
[2] Univ La Frontera, Dept Chem Engn, Temuco, Chile
[3] Tsing Hua Univ, Dept Environm Engn, Beijing 100084, Peoples R China
[4] Inst Politecn Nacl, CINVESTAV, Dept Biotechnol, Mexico City 07000, DF, Mexico
关键词
formaldehyde; urea; toxicity; anaerobic treatment; UASB reactors; adhesives manufacturing wastewaters;
D O I
10.1016/S0960-8524(99)00031-0
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The toxicity of formaldehyde (FA) in batch assays, using volatile fatty acids (VFA) as co-substrate, and the continuous anaerobic treatment of wastewaters containing FA in upflow anaerobic sludge blanket (UASB) reactors was investigated. In batch studies, FA exerted a 50% methanogenic toxicity on VFA at concentrations of around 100 mg/l, 2.5 times lower than values reported with sucrose. Although at FA concentrations higher than 200 mg/l methanogenesis was completely inhibited, a partial recovery of the bacterial activity was observed after 250 h when the FA had been removed from the medium. The continuous anaerobic degradation of FA at concentrations up to 2 g/l, using 1.6 g/l of glucose as co-substrate,was studied in a UASB reactor. A stable and efficient operation was observed at organic loading rates (OLR) of 6.0 g COD/l.d and with a COD/FA ratio as low as 1.4. A synthetic substrate with the same characteristics as the effluents produced during fibreboard adhesives manufacturing (based on urea-FA), i.e. 0.95 g FA/I and 0.35 g urea/l, was treated in a UASB reactor. The applied OLR and nitrogen loading rate (NLR) were 3.45 g COD/l.d and 0.58 g N/l.d, respectively. COD removal efficiencies were maintained at 90-95%, FA and urea being completely degraded. (C) 1999 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:283 / 291
页数:9
相关论文
共 30 条
[1]  
[Anonymous], STAND METH EX WAT WA
[2]   EFFLUENT TOXICITY TESTING USING NITRIFIERS AND MICROTOX(TM) [J].
ARBUCKLE, WB ;
ALLEMAN, JE .
WATER ENVIRONMENT RESEARCH, 1992, 64 (03) :263-267
[3]  
BHATTACHARYA SK, 1988, J WATER POLLUT CON F, V60, P531
[4]  
CHOU W, 1987, PROGRAM WATER TECHNO, V10, P545
[5]  
CVETKOVIC Z, 1988, CHEM BIOCHEM ENG Q, V2, P262
[6]   INFLUENCE OF HIGH NACL AND NH4CL SALT LEVELS ON METHANOGENIC ASSOCIATIONS [J].
DEBAERE, LA ;
DEVOCHT, M ;
VANASSCHE, P ;
VERSTRAETE, W .
WATER RESEARCH, 1984, 18 (05) :543-548
[7]  
DEBEKKER P, 1983, AN WAST WAT TREATM E, P449
[8]   Treatment of saline wastewaters from fish meal factories in an anaerobic filter under extreme ammonia concentrations [J].
Guerrero, L ;
Omil, F ;
Mendez, R ;
Lema, JM .
BIORESOURCE TECHNOLOGY, 1997, 61 (01) :69-78
[9]   THE EFFECTS OF ORGANIC TOXICANTS ON METHANE PRODUCTION AND HYDROGEN GAS LEVELS DURING THE ANAEROBIC-DIGESTION OF WASTE ACTIVATED-SLUDGE [J].
HICKEY, RF ;
VANDERWIELEN, J ;
SWITZENBAUM, MS .
WATER RESEARCH, 1987, 21 (11) :1417-1427
[10]  
IZA J, 1991, WATER SCI TECHNOL, V24, P1