Complete decomposition of biological waste sludge by thermophilic aerobic bacteria

被引:27
作者
Sakai, Y
Aoyagi, T
Shiota, N
Akashi, A
Hasegawa, S
机构
[1] Japan Sewage Works Agcy, Res & Technol Dev Div, Toda, Saitama 3350037, Japan
[2] Sewage Div Nakanojo Town, Gunma 3770494, Japan
[3] Shinko Pantec Co Ltd, Dept Res & Dev, Nishi Ku, Kobe, Hyogo 6512241, Japan
关键词
activated sludge process; enzyme; sludge; solubilization; thermophilic bacteria;
D O I
10.2166/wst.2000.0176
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Conventional activated sludge (AS) process is an economical and effective biooxidation process although a large amount of excess sludge is necessarily generated. We have developed a new zero-discharge AS process, in which no excess sludge is generated. It was formed by combining the conventional AS process with thermophilic aerobic sludge digester in which excess sludge is solubilized by thermophilic enzyme, so we call it hereafter the digester S-TE reactor. The excess sludge withdrawn from the AS step is subjected to the S-TE reactor, followed by its circulation to an aeration tank. Complete decomposition of the excess sludge is carried out when the sludge is solubilized by thermophilic aerobic bacteria (e.g. Bacillus sp.) and mineralized by mesophilic bacteria. The S-TE reactor is operated at 65 degreesC with hydraulic retention time of 1 day. Bench-scale test facilities of both the new process and conventional AS process were comparatively operated under the conditions of BOD-SS loading of 0.3 kg/kg/d and MLSS of 2,000 mg/L using artificial wastewater for over 100 days. The S-TE reactor was initially inoculated with the seedling culture of isolated Bacillus sp. bacteria. No additional inoculation seem to be needed under the steady condition since these bacteria can form spores and survive even under mesophilic conditions. The average rates of VSS solubilization and VM removal in the S-TE reactor were 40% and 15%, respectively. No excess sludge was generated when 3-fold amounts of the excess sludge generated in the conventional AS process were subjected to the S-TE reactor. in the new process, BOD was removed with high efficiency. Slight increase of SS and TOC was observed when compared with those of the AS process. A pilot-scale facility of the process has been operated with a petrochemical plant wastewater for a year. MLSS concentration was continuously kept around 3,000 mg/L without withdrawing the excess sludge. Inorganic salts seemed not to accumulate in the process. Therefore, it was demonstrated that excess sludge generation was completely reduced in the new process. According to our estimates, total operating costs for the new process are reduced to 40-50% of those of the conventional wastewater dewatering process. An application to a municipal sewage sludge treatment is currently performed in its full-scale facility.
引用
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页码:81 / 88
页数:8
相关论文
共 5 条
[1]   DEVELOPMENT OF HIGH-PERFORMANCE THERMOPHILIC 2-PHASE DIGESTION PROCESS [J].
AOKI, N ;
KAWASE, M .
WATER SCIENCE AND TECHNOLOGY, 1991, 23 (7-9) :1147-1156
[2]   AEROBIC DIGESTION OF ORGANIC SLUDGES [J].
ECKENFELDER, WW .
ENVIRONMENTAL TECHNOLOGY LETTERS, 1980, 1 (12) :537-546
[3]  
GAUDY AF, 1984, FUNDAMENTAL CONCEPTS
[4]   UPGRADING OF ANAEROBIC-DIGESTION OF WASTE ACTIVATED-SLUDGE BY THERMAL PRETREATMENT [J].
LI, YY ;
NOIKE, T .
WATER SCIENCE AND TECHNOLOGY, 1992, 26 (3-4) :857-866
[5]   FINITE-ELEMENT ANALYSIS OF 2 OVERCORING TECHNIQUES FOR INSITU STRESS MEASUREMENT [J].
WANG, Y ;
WONG, TF .
INTERNATIONAL JOURNAL OF ROCK MECHANICS AND MINING SCIENCES & GEOMECHANICS ABSTRACTS, 1987, 24 (01) :41-52