Future perspectives in bioreactor development

被引:26
作者
Mulder, R [1 ]
Vereijken, TLFM [1 ]
Frijters, CTMJ [1 ]
Vellinga, SHJ [1 ]
机构
[1] PAQUES Water Syst BV, NL-8560 AB Balk, Netherlands
关键词
aerobic; anaerobic; conversion rate; fluidised bed; granules; growth kinetics; psychrophilic; thermophilic; UASB;
D O I
10.2166/wst.2001.0457
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The paper discusses conversion capacities of both anaerobic and aerobic wastewater treatment systems in relation to growth kinetics, hydrodynamics and biomass concentration. In the current modern anaerobic high-rate reactors the conversion potentials are optimally exploited. This is not yet true for aerobic systems since operation of aerobic systems under conditions of low biomass growth reduces the maximum applicable loading rates significantly. Both the concept of granulation and the introduction of fluidised bed systems have increased conversion capacities for both anaerobic and aerobic systems significantly. One of the latest development concerns the SBR with granular biomass. The grazing concept, in which ciliates convert aerobically grown dispersed cells, offers a possibility for significant improvement of aerobic systems. In the fields of psychrophilic and thermophilic anaerobic treatment, specific reactor development may contribute to further enhance volumetric conversion capacities. Due to reduced water usage, both COD and salt concentrations tend to increase for industrial effluents. As a consequence, there is a need for the development of anaerobic reactors retaining flocculant biomass. The membrane bioreactors offer a solution for certain niches in wastewater treatment. However the oxygen transfer economy is poor. There is a need for fundamental knowledge development to obtain a realistic image of this technology.
引用
收藏
页码:27 / 32
页数:6
相关论文
共 15 条
[1]   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
[2]   APPLICATION OF THE BIOBED(R) UPFLOW FLUIDIZED-BED PROCESS FOR ANAEROBIC WASTE-WATER TREATMENT [J].
FRANKIN, RJ ;
KOEVOETS, WAA ;
VANGILS, WMA ;
VANDERPAS, A .
WATER SCIENCE AND TECHNOLOGY, 1992, 25 (07) :373-382
[3]   Extensive nitrogen removal in a new type of airlift reactor [J].
Frijters, CTMJ ;
Vellinga, S ;
Jorna, T ;
Mulder, R .
WATER SCIENCE AND TECHNOLOGY, 2000, 41 (4-5) :469-476
[4]   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
[5]   DEVELOPMENT AND SCALE-UP OF AN AEROBIC BIOFILM AIRLIFT SUSPENSION REACTOR [J].
HEIJNEN, JJ ;
VANLOOSDRECHT, MCM ;
MULDER, R ;
WELTEVREDE, R ;
MULDER, A .
WATER SCIENCE AND TECHNOLOGY, 1993, 27 (5-6) :253-261
[6]  
Henze M., 1987, ACTIVATED SLUDGE MOD
[7]  
Hulshoff Pol L. W., 1989, THESIS WAGENINGEN AG
[8]   USE OF THE UPFLOW SLUDGE BLANKET (USB) REACTOR CONCEPT FOR BIOLOGICAL WASTEWATER-TREATMENT, ESPECIALLY FOR ANAEROBIC TREATMENT [J].
LETTINGA, G ;
VANVELSEN, AFM ;
HOBMA, SW ;
DEZEEUW, W ;
KLAPWIJK, A .
BIOTECHNOLOGY AND BIOENGINEERING, 1980, 22 (04) :699-734
[9]  
MULDER R, 1990, THESIS U AMSTERDAM A
[10]  
REBAC S, 1998, THESIS WAGENINGEN AG