Effect of the organic loading rate on the performance of anaerobic acidogenic fermentation of two-phase olive mill solid residue

被引:54
作者
Rincon, B. [1 ]
Sanchez, E. [1 ]
Raposo, F. [1 ]
Borja, R. [1 ]
Travieso, L. [1 ]
Martin, M. A. [2 ]
Martin, A. [2 ]
机构
[1] CSIC, Inst Grasa, Seville 41012, Spain
[2] Fac Ciencias, Dept Ingn Quim, Cordoba 14071, Spain
关键词
D O I
10.1016/j.wasman.2007.02.030
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A study of the effect of the organic loading rate (OLR) on the anaerobic acidogenic fermentation of two-phase olive mill solid residue (OMSR) derived from fruits with a low ripening index was carried out in a laboratory-scale completely stirred tank reactor at mesophilic temperature (35 degrees C). Eight experimental runs were carried out at OLRs of 3.2, 5.6, 7.4, 9.6, 11.0, 12.9, 14.0 and 15.1 g T-COD/l d, which were equivalent to hydraulic retention times of 50.0, 28.8, 21.8 16.9, 14.7 12.4, 11.5 and 10.7 d, respectively. The experimental results obtained demonstrated that the optimum value of OLR for the acidogenic fermentation process was 12.9 g T-COD/l d, for which a maximum production of acetic acid was achieved. It was found that inhib ion of the process occurred at OLRs higher than 12.9 g T-COD/ I d. This was characterized by a significant decrease in the acetic acid concentration in the effluent and an increase in the concentration of other volatile acids that may affect the methanogenic step. The process inhibition was also characterized by the plateau in the curves of the effluent substrate concentration versus the OLR applied. It was found that a first-order kinetics satisfactorily described the influence of non-acetic acid soluble organic matter concentration (S-COD*) on the rate of soluble organic matter conversion to acetic acid (RS-COD*), and the influence of acetic acid concentration (AcH) on the rate of acetic acid production (R-AcH), while a potential equation type adequately described the influence of acetic acid concentration on the volumetric hydrogen production (Q(H2)). The kinetic constant for soluble organic matter removal was 0.145 d(-1), while the constant for acetic acid formation was found to be 0.075 d(-1). (C) 2007 Elsevier Ltd. All rights reserved.
引用
收藏
页码:870 / 877
页数:8
相关论文
共 23 条
[1]  
APHA-AWWA-WPCF, 1989, STAND METH EX WAT WA
[2]   The effect of addition of potato-processing wastewater on the acidogenesis of primary sludge under varied hydraulic retention time and temperature [J].
Banerjee, A ;
Elefsiniotis, P ;
Tuhtar, D .
JOURNAL OF BIOTECHNOLOGY, 1999, 72 (03) :203-212
[3]   Modelling of two-stage anaerobic digestion using the IWA Anaerobic Digestion Model No. 1 (ADM1) [J].
Blumensaat, F ;
Keller, J .
WATER RESEARCH, 2005, 39 (01) :171-183
[4]   Kinetic modelling of the hydrolysis, acidogenic and methanogenic steps in the anaerobic digestion of two-phase olive pomace (TPOP) [J].
Borja, R ;
Martín, A ;
Sánchez, E ;
Rincón, B ;
Raposo, F .
PROCESS BIOCHEMISTRY, 2005, 40 (05) :1841-1847
[5]   Study and optimisation of the anaerobic acidogenic fermentation of two-phase olive pomace [J].
Borja, R ;
Sánchez, E ;
Rincón, B ;
Raposo, F ;
Martín, MA ;
Martín, A .
PROCESS BIOCHEMISTRY, 2005, 40 (01) :281-291
[6]  
DINSDALE RM, 2000, BIORESOURCE TECHNOLO, V28, P870
[7]   Mesophilic acidification of gelatinaceous wastewater [J].
Fang, HHP ;
Yu, HQ .
JOURNAL OF BIOTECHNOLOGY, 2002, 93 (02) :99-108
[8]   Anaerobic hydrolysis of primary sludge: influence of sludge concentration and temperature [J].
Ferreiro, N ;
Soto, M .
WATER SCIENCE AND TECHNOLOGY, 2003, 47 (12) :239-246
[9]   Use of response surface analysis in selective bioconversion of starch wastewater to acetic acid using a mixed culture of anaerobes [J].
Lee, SY ;
Yang, KY ;
Hwang, SH .
PROCESS BIOCHEMISTRY, 2004, 39 (09) :1131-1135
[10]   Microbial community dynamics during start-up of acidogenic anaerobic reactors [J].
Liu, WT ;
Chan, OC ;
Fang, HHP .
WATER RESEARCH, 2002, 36 (13) :3203-3210