Development of anaerobic migrating blanket reactor (AMBR), a novel anaerobic treatment system

被引:124
作者
Angenent, LT [1 ]
Sung, SW [1 ]
机构
[1] Iowa State Univ, Dept Civil & Construct Engn, Ames, IA USA
关键词
anaerobic; anaerobic migrating blanket reactor; upflow anaerobic sludge blanket reactor; anaerobic sequencing batch reactor; granulation; methanogenesis;
D O I
10.1016/S0043-1354(00)00447-4
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A novel anaerobic treatment system, the anaerobic migrating blanket reactor (AMBR), was developed after completing a parallel study with upflow anaerobic sludge blanket (UASB) and anaerobic sequencing batch reactor (ASBR) processes. Using sucrose as the main component of a synthetic wastewater, the AMBR achieved a maximum chemical oxygen demand (COD) loading rate of 30 g.l(-1).day(-1) at a 12-h hydraulic retention time (HRT). This resulted in a standard methane production rate (SMPR) of 6.5 l.l(-1).day(-1) and an average methane-based COD (MCOD) removal efficiency of 62.2%. A key element in granular biomass formation was migration of the biomass blanket through the reactor. Although a carbohydrate-rich wastewater was used, no separate pre-acidification was required for the AMBR, because of high mixing intensities and wash out of acidogenic bacteria. In contrast, the absence of pre-acidification created "bulking" problems (caused by abundant acidogenic bacteria at the surface of granules) in a UASB reactor, operated under conditions similar to that of the AMBR. As a result, a maximum COD loading rate and SMPR of 21 g.l(-1).day(-1) and 4.9 l.l(-1).day(-1) were achieved, respectively, for the UASB reactor at a 12-h HRT. These values were 18 g.l(-1).day(-1) and 3.7 l.l(-1).day(-1), respectively, for an ASBR at a 12-h HRT. Hence, the performance of the AMBR in treating a carbohydrate-rich wastewater was found to be superior in terms of maximum loading rate and SMPR. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:1739 / 1747
页数:9
相关论文
共 23 条
  • [1] Alphenaar P.A., 1994, THESIS WAGENINGEN AG
  • [2] Angenent L. T., 1996, Mededelingen Faculteit Landbouwkundige en Toegepaste Biologische Wetenschappen Universiteit Gent, V61, P2077
  • [3] ANGENENT LT, 1995, P 50 PURD IND WAST C, P365
  • [4] APHA, 1985, STAND METH EX WAT WA
  • [5] Bachman A., 1982, P 1 INT C FIX FILM B, P1192
  • [6] PERFORMANCE-CHARACTERISTICS OF THE ANAEROBIC BAFFLED REACTOR
    BACHMANN, A
    BEARD, VL
    MCCARTY, PL
    [J]. WATER RESEARCH, 1985, 19 (01) : 99 - 106
  • [7] CONTACT-ANGLE MEASUREMENT AND CELL HYDROPHOBICITY OF GRANULAR SLUDGE FROM UPFLOW ANAEROBIC SLUDGE BED REACTORS
    DAFFONCHIO, D
    THAVEESRI, J
    VERSTRAETE, W
    [J]. APPLIED AND ENVIRONMENTAL MICROBIOLOGY, 1995, 61 (10) : 3676 - 3680
  • [8] ANAEROBIC TREATMENT APPLICATIONS AND FUNDAMENTALS - SUBSTRATE-SPECIFICITY DURING PHASE-SEPARATION
    FOX, P
    POHLAND, FG
    [J]. WATER ENVIRONMENT RESEARCH, 1994, 66 (05) : 716 - 724
  • [9] ROLE OF SUBSTRATE CONCENTRATION IN PARTICLE-SIZE DISTRIBUTION OF METHANOGENIC ANTIGRANULOCYTES SLUDGE IN UASB REACTORS
    GROTENHUIS, JTC
    KISSEL, JC
    PLUGGE, CM
    STAMS, AJM
    ZEHNDER, AJB
    [J]. WATER RESEARCH, 1991, 25 (01) : 21 - 27
  • [10] GUIOT SR, 1992, WATER SCI TECHNOL, V25, P1