Long term operation of a thermophilic anaerobic reactor: Process stability and efficiency at decreasing sludge retention time

被引:138
作者
Ferrer, Ivet [1 ,2 ]
Vazquez, Felicitas [3 ]
Font, Xavier [4 ]
机构
[1] Tech Univ Catalonia, Dept Hydraul Maritime & Environm Engn, Environm Engn Div, UPC, E-08034 Barcelona, Spain
[2] GIRO Technol Ctr, Barcelona 08100, Spain
[3] Univ Autonoma Barcelona, Inst Biotechnol & Biomed, E-08193 Barcelona, Spain
[4] Univ Autonoma Barcelona, Composting Res Grp, Dept Chem Engn, Escola Tecn Super Engn, E-08193 Barcelona, Spain
关键词
Biogas; Biosolids; Dewaterability; Hygienisation; Wastewater; ACTIVATED-SLUDGE; SEWAGE-SLUDGE; START-UP; DIGESTION; PRETREATMENT; TEMPERATURE; PERFORMANCE; HYDROLYSIS; AMMONIA; PH;
D O I
10.1016/j.biortech.2009.12.006
中图分类号
S2 [农业工程];
学科分类号
082806 [农业信息与电气工程];
摘要
The aim of this Study was to evaluate the performance of thermophilic sludge digestion at decreasing sludge retention time (SRT) and increasing organic loading rate (OLR), in terms of methane production, effluent stabilisation, hygienisation and dewaterability. Focus Was Put on determining indicators to help prevent process failure. To this end, a lab-scale reactor was operated for nearly 2 years at 55 degrees C. Methane production rate was increased (from 0.2 to 0.4-0.6 m(CH4)(3) m(reactor)(-3) d(-1)) by decreasing the SRT from 30 to 15-10 days, while increasing the OLR from 0 5 to 2.5-3.5 kg VS m(reactor)(-3) d(-1). Sludge dewaterability was worsened at SRT below 15 days; while pathogen destruction was always successful. The following concentrations might be used to prevent process failure: VFA C2-C5 (3.7 g COD L-1), acetate (0.6 g L-1), acetate/propionate (0.5), intermediate alkalinity (1.8 g CaCO3 L-1), inteFniediate/partial alkalinity (0.9), intermediate/total alkalinity (0.5), CH4 in biogas (55%). (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2972 / 2980
页数:9
相关论文
共 35 条
[1]
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
[2]
ANAEROBIC THERMOPHILIC DIGESTION OF MANURE AT DIFFERENT AMMONIA LOADS - EFFECT OF TEMPERATURE [J].
ANGELIDAKI, I ;
AHRING, BK .
WATER RESEARCH, 1994, 28 (03) :727-731
[3]
[Anonymous], 2003, WAST ENG TREATM REUS
[4]
[Anonymous], 1999, Standard Methods for Examination of Water and Waste Water
[5]
Air stripping of ammonia from pig slurry:: characterisation and feasibility as a pre- or post-treatment to mesophilic anaerobic digestion [J].
Bonmatí, A ;
Flotats, X .
WASTE MANAGEMENT, 2003, 23 (03) :261-272
[6]
THERMOPHILIC ANAEROBIC DIGESTION PROCESS [J].
BUHR, HO ;
ANDREWS, JF .
WATER RESEARCH, 1977, 11 (02) :129-143
[7]
Effect of solids retention time (SRT) on pilot scale anaerobic thermophilic sludge digestion [J].
de la Rubia, MA ;
Perez, M ;
Romero, LI ;
Sales, D .
PROCESS BIOCHEMISTRY, 2006, 41 (01) :79-86
[8]
Pilot-scale anaerobic thermophilic digester treating municipal sludge [J].
de la Rubia, MA ;
Romero, LI ;
Sales, D ;
Perez, M .
AICHE JOURNAL, 2006, 52 (01) :402-407
[9]
de la Rubia MA, 2002, CHEM BIOCHEM ENG Q, V16, P119
[10]
Effect of ultrasound pretreatment in mesophilic and thermophilic anaerobic digestion with emphasis on naphthalene and pyrene removal [J].
El-Hadj, T. Benabdallah ;
Dosta, J. ;
Marquez-Serrano, R. ;
Mata-Alvarez, J. .
WATER RESEARCH, 2007, 41 (01) :87-94