Effect of organic loading rate on aerobic granulation. I: Reactor performance

被引:101
作者
Tay, JH [1 ]
Pan, S [1 ]
He, YX [1 ]
Tay, STL [1 ]
机构
[1] Nanyang Technol Univ, Sch Civil & Environm Engn, Div Environm & Water Resources Engn, Singapore 639798, Singapore
关键词
organic loads; cisterns; sludge; biomass; wastewater treatment;
D O I
10.1061/(ASCE)0733-9372(2004)130:10(1094)
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The effect of organic loading rate (OLR) on the aerobic granulation process was investigated using laboratory-scale sequential aerobic sludge blanket reactors (SASBRs). Reactors R1, R2, R3, and R4 were operated at OLRs of 1, 2, 4 and 8 kg chemical oxygen demand (COD)/m(3) day, respectively. Aerobic granules could not be formed at the relatively low OLRs in RI and R2. Stable aerobic granules were successfully cultivated at the mid-range OLR of 4 kg COD/m(3) day tested in Reactor R3. These granules first appeared 14 days after startup and eventually grew to become the dominant form of biomass in R3. The granular biomass stabilized at a mixed liquor volatile suspended solids (MLVSS) concentration of 12,000 mg/L, with a food-to-microorganism (F/M) ratio of 0.33 kg COD/kg MLVSS day and a mean cell residence time of 31.1 days. Aerobic granules were first observed on Day 18 in Reactor R4, which operated at the highest OLR tested of 8 kg COD/m(3) day. However, these granules were unstable and eventually washed out of R4. The best reactor performance was achieved in R3 with a COD removal rate of 99%, an observed yield coefficient Won) of 0.10 mg MLVSS/mg COD, and a sludge volume index 24 mL/g MLVSS. The volumetric specific oxygen utilization rate was highest in R3, at 356 mg O-2/L h. An optimal choice of OLR was found to favor the cultivation and retention of well-settling granules and enhanced the overall ability of the reactor to remove COD. This study contributes to a better understanding of the role of OLR in aerobic granulation.
引用
收藏
页码:1094 / 1101
页数:8
相关论文
共 45 条
[1]  
[Anonymous], 1995, STANDARD METHODS EXA, V19th
[2]  
[Anonymous], 1983, WATER SCI TECHNOL, DOI DOI 10.2166/wst.1983.0172
[3]  
BARBOUR D, 1995, TCI, V29, P7
[4]  
BEEFTINK HH, 1987, THESIS U AMSTERDAM A
[5]   Aerobic granulation in a sequencing batch reactor [J].
Beun, JJ ;
Hendriks, A ;
Van Loosdrecht, MCM ;
Morgenroth, E ;
Wilderer, PA ;
Heijnen, JJ .
WATER RESEARCH, 1999, 33 (10) :2283-2290
[6]   Triggers for microbial aggregation in activated sludge? [J].
Bossier, P ;
Verstraete, W .
APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1996, 45 (1-2) :1-6
[7]   BIOFILM DETACHMENT MECHANISMS IN A LIQUID-FLUIDIZED BED [J].
CHANG, HT ;
RITTMANN, BE ;
AMAR, D ;
HEIM, R ;
EHLINGER, O ;
LESTY, Y .
BIOTECHNOLOGY AND BIOENGINEERING, 1991, 38 (05) :499-506
[8]   MICROELECTRODE MEASUREMENTS OF THE ACTIVITY DISTRIBUTION IN NITRIFYING BACTERIAL AGGREGATES [J].
DEBEER, D ;
VANDENHEUVEL, JC ;
OTTENGRAF, SPP .
APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 1993, 59 (02) :573-579
[9]   CHARACTERISTICS OF GRANULAR METHANOGENIC SLUDGE GROWN ON LACTATE IN A UASB REACTOR [J].
FUKUZAKI, S ;
CHANG, YJ ;
NISHIO, N ;
NAGAI, S .
JOURNAL OF FERMENTATION AND BIOENGINEERING, 1991, 72 (06) :465-472
[10]   FORMATION OF BIOFILMS IN A BIOFILM AIRLIFT SUSPENSION REACTOR [J].
HEIJNEN, JJ ;
VANLOOSDRECHT, MCM ;
MULDER, A ;
TIJHUIS, L .
WATER SCIENCE AND TECHNOLOGY, 1992, 26 (3-4) :647-654