Scale-up and cost evaluation of a foamed emulsion bioreactor

被引:4
|
作者
Kan, E. [1 ]
Deshusses, M. A. [1 ]
机构
[1] Univ Calif Riverside, Dept Chem & Environm Engn, Riverside, CA 92521 USA
关键词
foamed emulsion bioreactor; air pollution control; biofilter; scale-up; cost evaluation;
D O I
10.1080/09593332708618675
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In the present paper, the potential of the foamed emulsion bioreactor (FEBR), a novel biological reactor for air pollution control was evaluated. Experimental data obtained on a laboratory-scale prototype were used to scale-up the process for a hypothetical case consisting of a contaminated air flow rate of 10,000 m(3) h(-1), a toluene inlet concentration of 1 g m(-3) and minimum required treatment efficiency of 92%. Reactor design and operating issues for the full-scale FEBR were identified. They included the requirement for stable foam generation with appropriate air distributors, and recycling of the auxiliary organic phase, surfactants and cells from the discharge of the reactor. The capital and operating costs for the concept full-scale FEBR were evaluated and compared to those of competing technologies, namely biofiltration, biotrickling filtration and catalytic and thermal oxidation. All three biological techniques had significantly lower capital and operating costs. Among the biological techniques, the FEBR had the lowest estimated capital cost since its greater effectiveness allowed a smaller reactor to meet the treatment objectives. The operating costs for the FEBR were higher than those of biofilters and biotrickling filters because of the requirements for nutrients and auxiliary chemicals. Overall, the results highlight that biotreatment is much more cost effective than thermal and catalytic oxidation. They further suggest that the FEBR may an interesting alternative to biofilters and biotrickling filters where the available space for air pollution control equipment is limited.
引用
收藏
页码:645 / 652
页数:8
相关论文
共 50 条
  • [1] SCALE-UP OF A CYCLONE BIOREACTOR
    SHEPPARD, JD
    MARCHESSAULT, P
    WHALEN, T
    BARRINGTON, SF
    [J]. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 1994, 59 (01) : 83 - 89
  • [2] PHYSIOLOGICAL SIMILARITY AND BIOREACTOR SCALE-UP
    VOTRUBA, J
    SOBOTKA, M
    [J]. FOLIA MICROBIOLOGICA, 1992, 37 (05) : 331 - 345
  • [3] SCALE-UP FOR A FLUIDIZED-BED BIOREACTOR
    MAFFIA, GJ
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1992, 203 : 101 - BIOT
  • [4] Practical approach in bioreactor scale-up and process transfer
    Xu, Sen
    Hoshan, Linda
    Jiang, Rubin
    Gupta, Balrina
    Brodean, Eric
    Bowers, John
    O'Neill, Kristin
    Seamans, T. Craig
    Chen, Hao
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2017, 253
  • [5] Mixing Characteristics for Scale-up of an Orbital Shaken Bioreactor
    Lee, Hyunwoo
    Lee, Joon-Chul
    Seo, Youngjin
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 2022, 45 (05) : 946 - 952
  • [6] Optimization and scale-up of bioreactor for mammalian cell culture
    Kamekura, Koichi
    Iso, Yoshiyuki
    Iwasa, Yoshitaka
    Ooki, Takamasa
    Sugaya, Kazuo
    [J]. JOURNAL OF BIOSCIENCE AND BIOENGINEERING, 2009, 108 : S7 - S7
  • [7] SIMPLIFYING SCALE-UP COST ESTIMATION
    CAPPELLO, VF
    [J]. CHEMICAL ENGINEERING, 1972, 79 (17) : 99 - &
  • [8] Development of a statistical model to support perfusion bioreactor scale-up
    Schwarz, Kelly
    Raley, Jonathan
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2018, 255
  • [9] A Scale-up System for Lowbush Blueberry Micropropagation Using a Bioreactor
    Debnath, Samir C.
    [J]. HORTSCIENCE, 2009, 44 (07) : 1962 - 1966
  • [10] SIMULATED SCALE-UP OF A YEAST FERMENTATION USING A LOOP BIOREACTOR
    MCNEIL, B
    KRISTIANSEN, B
    [J]. BIOTECHNOLOGY LETTERS, 1990, 12 (01) : 39 - 44