• 제목/요약/키워드: Blofilter

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VOC 처리를 위한 Biofilter 개발 원리 및 상업화 (Principle and Commercialization of Biofilter for Treatment of Volatile Organic Compounds)

  • 이은열;황재웅;강염석;문철연;박성훈
    • 한국생물공학회:학술대회논문집
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    • 한국생물공학회 2004년도 학술대회지
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    • pp.85-106
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    • 2004
  • Styrene as volatile organic compounds(VOC) has come under strict regulatory control as they cause serious health and environmental problems. Biofiltration offers a number of economical and environmental advantages over conventional technologies, such as incineration, catalytic adsorption, and chemical scrubbing. In this presentation, recent progresses on the development of lab-scale biofilter for the treatment of gas-phase styrene are reviewed, The potentials of commercialization of biofilter systems are also discussed.

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해수 조건에서 모래유동층 여과조의 TAN 부하량과 수온에 따른 질산화 효율 (Nitrification Efficiency of the Fluidized Sand Biofilter by TAN Leading Rates and Temperatures in the Simulated Seawater Aquaculture Condition)

  • 박정환
    • 한국수산과학회지
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    • 제38권6호
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    • pp.347-352
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    • 2005
  • These experiments investigated the conditioning pattern and the nitrification efficiency of a fluidized sand biofilter (FSB) for seawater application. The FSB fed artificial nutrient was fully conditioned within 22 weeks. The maximum nitrification efficiency of the FSB was achieved at a superficial water velocity (SWV) of 1.0 cm/sec. After fixing the superficial water velocity at 1.0 cm/sec, the nitrification rates of the FSB were assessed at 3 total ammonia nitrogen (TAN) loading rates (250, 500, 1,000 g TAN/$m^3$/day) and 3 water temperatures (12, 16, $20^{\circ}C$). The TAN concentration in the simulated culture tank ranged from 2.87 to 9.72 mg/L at TAN loading rate of 1,000 g TAN/$m^3$/day, while that ranged from 0.45 to 1.26 mg/L at TAN loading rate of 500 g TAN/$m^3$/day. The ranges of TAN concentration in the former were too high for aquatic organisms and those in the latter were acceptable. Therefore, the safe TAN loading rate for the FSB in seawater conditions was decided as 500 g TA/$m^3$/day. From these results, daily TAN removal rates (g TAN/$m^3$/day) of FSB under conditions of inlet TAN concentration (C, mg/L) and water temperature (T, $^{\circ}C$) were calculated by the following non-linear multi-regression equation: TAN removal rate: f(z)=-1,311.295+655.714LnT+225.775LnC ($r^2=0.962$).