Optimisation of the anaerobic digestion of agricultural resources

被引:1080
作者
Ward, Alastair J. [1 ,2 ]
Hobbs, Phil J. [2 ]
Holliman, Peter J. [1 ]
Jones, David L. [3 ]
机构
[1] Univ Wales, Sch Chem, Bangor LL57 2UW, Gwynedd, Wales
[2] Inst Grassland & Environm Res, Okehampton EX20 2SB, Devon, England
[3] Univ Wales, Sch Environm & Nat Resources, Bangor LL57 2UW, Gwynedd, Wales
关键词
anaerobic digestion; biomass; optimisation; process control; review;
D O I
10.1016/j.biortech.2008.02.044
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
It is in the interest of operators of anaerobic digestion plants to maximise methane production whilst concomitantly reducing the chemical oxygen demand of the digested material. Although the production of biogas through anaerobic digestion is not a new idea, commercial anaerobic digestion processes are often operated at well below their optimal performance due to a variety of factors. This paper reviews current optimisation techniques associated with anaerobic digestion and suggests possible areas where improvements could be made, including the basic design considerations of a single or multi-stage reactor configuration, the type, power and duration of the mixing regime and the retention of active microbial biomass within the reactor. Optimisation of environmental conditions within the digester such as temperature, pH, buffering capacity and fatty acid concentrations is also discussed. The methane-producing potential of various agriculturally sourced feedstocks has been examined, as has the advantages of codigestion to improve carbon-to-nitrogen ratios and the use of pre-treatments and additives to improve hydrolysis rates or supplement essential nutrients which may be limiting. However, perhaps the greatest shortfall in biogas production is the lack of reliable sensory equipment to monitor key parameters and suitable, parallelised control systems to ensure that the process continually operates at optimal performance. Modern techniques such as software sensors and powerful, flexible controllers are capable of solving these problems. A direct comparison can be made here with, for instance, oil refineries where a more mature technology uses continuous in situ monitoring and associated feedback procedures to routinely deliver continuous, optimal performance. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:7928 / 7940
页数:13
相关论文
共 174 条
[31]  
Chanakya HN, 1998, CURR SCI INDIA, V74, P1054
[32]   Structural and functional characterization of a novel phosphodiesterase from Methanococcus jannaschii [J].
Chen, SF ;
Yakunin, AF ;
Kuznetsova, E ;
Busso, D ;
Pufan, R ;
Proudfoot, M ;
Kim, R ;
Kim, SH .
JOURNAL OF BIOLOGICAL CHEMISTRY, 2004, 279 (30) :31854-31862
[33]   BIOCHEMICAL METHANE POTENTIAL AND SOLID-STATE ANAEROBIC-DIGESTION OF KOREAN FOOD WASTES [J].
CHO, JK ;
PARK, SC ;
CHANG, HN .
BIORESOURCE TECHNOLOGY, 1995, 52 (03) :245-253
[34]   BIOCHEMICAL METHANE POTENTIAL OF BIOMASS AND WASTE FEEDSTOCKS [J].
CHYNOWETH, DP ;
TURICK, CE ;
OWENS, JM ;
JERGER, DE ;
PECK, MW .
BIOMASS & BIOENERGY, 1993, 5 (01) :95-111
[35]   Bench-scale anaerobic bioconversion of newsprint and office paper [J].
Clarkson, WW ;
Xiao, W .
WATER SCIENCE AND TECHNOLOGY, 2000, 41 (03) :93-100
[36]   Simple method for the measurement of the hydrogenotrophic methanogenic activity of anaerobic sludges [J].
Coates, JD ;
Coughlan, MF ;
Colleran, E .
JOURNAL OF MICROBIOLOGICAL METHODS, 1996, 26 (03) :237-246
[37]  
CordRuwisch R, 1997, BIOTECHNOL BIOENG, V56, P626, DOI 10.1002/(SICI)1097-0290(19971220)56:6<626::AID-BIT5>3.0.CO
[38]  
2-P
[39]   Effects of feeding time and organic loading in an anaerobic sequencing batch biofilm reactor (ASBBR) treating diluted whey [J].
Damasceno, Leonardo H. S. ;
Rodrigues, Jose A. D. ;
Ratusznei, Suzana M. ;
Zaiat, Marcelo ;
Foresti, Eugenio .
JOURNAL OF ENVIRONMENTAL MANAGEMENT, 2007, 85 (04) :927-935
[40]   Anaerobic digestion of solid waste: state-of-the-art [J].
De Baere, L .
WATER SCIENCE AND TECHNOLOGY, 2000, 41 (03) :283-290