Laboratory investigations on continuous bio-methanization of energy crops as mono-substrate without supplementation

被引:4
作者
Demirel, Burak [1 ,2 ]
机构
[1] Bogazici Univ, Inst Environm Sci, TR-34342 Istanbul, Turkey
[2] Hamburg Univ Appl Sci, HAW Hamburg, D-21033 Hamburg, Germany
关键词
Anaerobic digestion; Beet silage; Beta vulgaris; Biogas; Energy crops; Fuzzy logic; Renewable energy; THERMOPHILIC ANAEROBIC-DIGESTION; MUNICIPAL SOLID-WASTE; FODDER BEET SILAGE; CO-DIGESTION; METHANE PRODUCTION; ORGANIC WASTES; MANURE; TEMPERATURE; PLANTS; RESIDUES;
D O I
10.1016/j.biombioe.2009.03.005
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Continuous bio-methanization of an energy crop, namely the beet silage, was investigated in this laboratory-scale work as mono-substrate, using a mesophilic biogas digester controlled by a fuzzy logic control (FLC) technique and without using any supplementing or buffering agent, despite the low pH of the substrate around 3.80. The temperature, pH, redox potential (ORP), daily biogas production and composition of digester biogas were continuously measured online. During the operation, the hydraulic retention time (HRT) varied between 24.8 and 9 days, as the organic loading rate (OLR) ranged from 2.6 to 4.7 g L (1) d (1). The average pH, specific gas production rate (spec. GPR) and volumetric gas production rate (vol. GPR) were determined to be 7.12, 0.31 L gVS(-1) d(-1) and 1.084 L L (1) d (1), respectively. The average methane (CH4) content of digester biogas was about 56%. The FLC technique, which was developed at HAW Hamburg for anaerobic conversion of acidic energy crops to methane, determined the daily feeding volume (similar to OLR/HRT) for the biogas digester, depending on the feedback from online pH and methane measurements, and on the calculation of the Spec. GPR. The Spec. GPR was calculated by the corrected daily biogas production. Through online monitoring of pH, biogas production rate and composition, and by use of the FLC technique, the acidic beet silage could continuously be converted to biogas, without using manure or any other kind of buffering or supplementing agent(s). The lab-scale anaerobic biogas digester performed stable and safe, without encountering any problems of instability, as indicated by an adequate amount of buffering capacity, a VFA content below 0.5 g L (1) and a neutral pH range throughout the study. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:988 / 993
页数:6
相关论文
共 54 条
[1]   METHANOGENESIS IN THERMOPHILIC BIOGAS REACTORS [J].
AHRING, BK .
ANTONIE VAN LEEUWENHOEK INTERNATIONAL JOURNAL OF GENERAL AND MOLECULAR MICROBIOLOGY, 1995, 67 (01) :91-102
[2]   Effect of temperature increase from 55 to 65°C on performance and microbial population dynamics of an anaerobic reactor treating cattle manure [J].
Ahring, BK ;
Ibrahim, AA ;
Mladenovska, Z .
WATER RESEARCH, 2001, 35 (10) :2446-2452
[3]   The effect of temperature variation on biomethanation at high altitude [J].
Alvarez, Rene ;
Liden, Gunnar .
BIORESOURCE TECHNOLOGY, 2008, 99 (15) :7278-7284
[4]  
ANGELIDAKI I, 1993, APPL MICROBIOL BIOT, V38, P560
[5]   Codigestion of manure and organic wastes in centralized biogas plants - Status and future trends [J].
Angelidaki, I ;
Ellegaard, L .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2003, 109 (1-3) :95-105
[6]  
[Anonymous], 1989, Standard Methods for Examination of water and waste water, V17th
[7]  
[Anonymous], 1985, 384148 DIN
[8]   Thermophilic anaerobic digester performance under different feed-loading frequency [J].
Bombardiere, John ;
Espinosa-Solares, Teodoro ;
Domaschko, Max ;
Chatfield, Mark .
APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 2007, 137 (1-12) :765-775
[9]   FUZZY CONTROL OF AN ANAEROBIC DIGESTER FOR THE TREATMENT OF THE ORGANIC FRACTION OF MUNICIPAL SOLID-WASTE (MSW) [J].
BOSCOLO, A ;
MANGIAVACCHI, C ;
DRIUS, F ;
RONGIONE, F ;
PAVAN, P ;
CECCHI, F .
WATER SCIENCE AND TECHNOLOGY, 1993, 27 (02) :57-68
[10]  
BRAUN R, 1981, BIOTECHNOL LETT, V3, P159