Hydrolytic pretreatment of oily wastewater by immobilized lipase

被引:48
作者
Jeganathan, Jeganaesan [1 ]
Nakhla, George [1 ]
Bassi, Amarjeet [1 ]
机构
[1] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON N6A 5B9, Canada
关键词
immobilized lipase; wastewater treatment; hydrolysis; oil and grease; anaerobic processes;
D O I
10.1016/j.jhazmat.2006.11.004
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The purpose of this study was to evaluate the hydrolysis of wastewater with high oil and grease (O&G) concentration from a pet food industry using immobilized lipase (IL) as a pretreatment step for anaerobic treatment through batch and continuous-flow experiments. The intrinsic Michaelis constant (K-m) and maximum reaction rate (V-max) were estimated experimentally and the K-m, value of IL (22.5 g O&G/L) was six-folds higher than that of the free lipase (FL) (3.6 g O&G/L), whereas V-max of both FL (31.3 mM/g min) and IL (33.1 mM/g min) were similar. Preliminary batch anaerobic respirometric experiments showed that chemical oxygen demand (COD) and O&G reduction were 49 and 45% without pretreatment and 65 and 64% with IL pretreatment respectively, while the maximum growth rate (mu(max)) for pretreated wastewater (0. 17 d(-1)) was 3.4-folds higher than that of raw wastewater (0.05 d(-1)) with similar Monod half-saturation constants (K-S similar to 2.7 g COD/L). The continuous-flow experimental study showed the feasibility of employing the hybrid packed bed reactor (PBR)-upflow anaerobic sludge blanket (UASB) system for the treatment of high-strength oily wastewater, as reflected by its ability to operate at an oil loading rate (LR) of 4.9 kg O&G/m(3) d (to the PBR) without any problems for a period of 100 days. During pseudo- steady-state conditions, the hybrid UASB produced relatively higher biogas compared to the control UASB, The effluent COD and O&G concentrations of hybrid system were 100 mg/L lower than that of the control UASB reactor and no foam production was observed in the hybrid UASB compared to the control UASB reactor. (c) 2006 Elsevier B.V. All rights reserved.
引用
收藏
页码:127 / 135
页数:9
相关论文
共 33 条
[1]  
[Anonymous], 1998, OFF METH REC PRACT, V5th
[2]  
[Anonymous], 1995, STANDARD METHODS EXA, V19th
[3]  
Benjamin S, 1998, YEAST, V14, P1069, DOI 10.1002/(SICI)1097-0061(19980915)14:12<1069::AID-YEA303>3.3.CO
[4]  
2-B
[5]   BIOCHEMICALLY ACTIVE SOL-GEL GLASSES - THE TRAPPING OF ENZYMES [J].
BRAUN, S ;
RAPPOPORT, S ;
ZUSMAN, R ;
AVNIR, D ;
OTTOLENGHI, M .
MATERIALS LETTERS, 1990, 10 (1-2) :1-5
[6]   Enzymatic pre-hydrolysis and anaerobic degradation of wastewaters with high fat contents [J].
Cammarota, MC ;
Teixeira, GA ;
Freire, DMG .
BIOTECHNOLOGY LETTERS, 2001, 23 (19) :1591-1595
[7]   Improved properties of bilirubin oxidase by entrapment in alginate-silicate sol-gel matrix [J].
Chen, JP ;
Wang, HY .
BIOTECHNOLOGY TECHNIQUES, 1998, 12 (11) :851-853
[8]   Immobilization of Candida rugosa lipase on chitosan with activation of the hydroxyl groups [J].
Chiou, SH ;
Wu, WT .
BIOMATERIALS, 2004, 25 (02) :197-204
[9]   Mesoporous alginate/silica biocomposites for enzyme immobilisation [J].
Coradin, T ;
Livage, J .
COMPTES RENDUS CHIMIE, 2003, 6 (01) :147-152
[10]   The kinetics of hydrolysis of animal fat by pancreatic lipase [J].
German, AB ;
Neklyudov, AD ;
Ivankin, AN ;
Berdutina, AV .
APPLIED BIOCHEMISTRY AND MICROBIOLOGY, 2002, 38 (06) :517-520