• 제목/요약/키워드: Waste bed

검색결과 255건 처리시간 0.024초

Removal Efficiency of the Pollutants from Piggery Wastes with Activated Carbon Treated with Metal and Their Pilot Scale Design

  • Oh, Won-Chun;Park, Chong-Sung;Bae, Jang-Soon;Ko, Young-Shin
    • Carbon letters
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    • 제7권3호
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    • pp.180-187
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    • 2006
  • The treatment of piggery wastes was carried out at pilot scale using a multilayered metal-activated carbon system followed by carbon bed filtration. The physicochemical properties were obtained from treated samples with aqueous solutions containing metallic ions such as $Ag^+$, $Cu^{2+}$, $Na^+$, $K^+$ and $Mn^{2+}$, which main obsevations are subjected to inspect surface properties, color removal properties by Uv/Vis and EDX. Multilayered metal-activated carbons were contacted with waste water to investigation of the simultaneous catalytic effect for the COD, BOD, T-N and T-P removal. The removal results for the piggery waste using multilayered metal-activated carbon bed was achieved the satisfactory removal performance under permitted values of Ministry of Environment of Korea. The high efficiency of the multilayered metal-activated carbon bed was determined by the performance of this material for trapping, catalytic effect and adsorption of organic solid particles.

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알루미늄 식각폐액의 응집 특성에 관한 연구 (A Study on The Coagulation Characteristics of The Aluminium Etching Waste)

  • 김준호;이창환;이철호
    • 청정기술
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    • 제10권1호
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    • pp.1-7
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    • 2004
  • 본 연구는 알루미늄 식각액(PWF100)이 응집제로서의 성능을 가지고 있는가를 평가하고 시중에서 판매되고 있는 응집제(PAC17)와의 물성을 비교하였다. PWF100을 이용하여 제조된 BKN-100, BKR-110, 그리고 BKR-120의 농도에 따른 침전층의 높이를 측정하였는데 농도가 낮은 범위에서는 첨가제의 농도가 증가할수록 침전층의 높이가 감소하지만 일정농도 이상에서는 침전층의 높이가 일정해졌다. BKN-100의 농도에 따른 침전층의 밀도를 조사하였는데 BKN-100의 농도가 증가에 따라 침전층의 밀도가 감소하는 경향이 있었다. BKN-100, BKR-110, 그리고 BKR-120 응집제의 첨가량에 따른 침강속도의 변화를 조사하였는데, 첨가량이 증가함에 따라서 침강속도가 빨라지지만 일정한 농도 이상에서는 침강속도가 둔화되었다. BKN-100, BKR-110, 그리고 BKR-120의 농도에 따른 침전층 형성시간의 변화를 측정하였는데, 저농도 영역에서는 농도가 증가함에 따라 침전층 형성시간이 감소하지만 일정농도 이상에서는 침전층 형성시간이 증가하였다. 위의 실험결과로부터 PWF100은 응집제로서의 효과가 있는 것으로 판정되었다.

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석탄 및 폐기물로부터 합성가스 제조를 위한 가스화용융 Pilot Plant 운전특성 (Operation Characteristics of Gasification/Melting Pilot Plants for Synthesis Gas Production using Coal and Waste)

  • 정석우;윤용승;유영돈
    • 한국신재생에너지학회:학술대회논문집
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    • 한국신재생에너지학회 2005년도 춘계학술대회
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    • pp.561-564
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    • 2005
  • Gasification has been regarded as a very important technology to decrease environmental pollution and to obtain higher efficiency. The gasification process converts carbon containing feedstock into a synthesis gas, composed primarily of CO and $H_2$. And the synthesis gas can be used as a source for power generation or chemical material production. Through more than nine years, IAE developed and upgraded several gasification/melting pilot plant system, and obtained a good quality synthesis gas. This paper illustrates the gasification characteristics and operation results of two 3 ton/day synthesis gas production facilities. One is entrained-bed slagging type coal gasifier system which is normally operated in the temperature range of $1,400\~1,450^{\circ}C,\;8\~10$ bar pressure. And the other is fixed-bed type gasification/melting furnace system using MSW and industrial wastes as a feedstock.

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VOCs 연소를 위한 자동차 폐촉매의 전처리 효과 (Pretreatment Effect of Waste Automotive Catalysts for VOCs Combustion)

  • 문정선
    • 한국대기환경학회지
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    • 제16권2호
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    • pp.191-198
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    • 2000
  • For a characterization of the pretreated waste automotive catalyst the following analysis techniques were applied : EA(Elemental Analysis) BET(Brunaure-Emmett-Teller) and ICP-AES(Inductively Coupled Plasma-Atomic Emission Spectrometry). The combustion activity of waste automotive catalyst was investigated for methanol acetaldehyde and toluene as model VOCs in a fixed bed reactor. carbon deposit amount was decreased with increasing catalyst showed a good catalytic activity for VOCs combustion at 40$0^{\circ}C$. Catalytic activity for methanol acetaldehyde and toluence combustion was very excellent and decreased with mileage. The catalytic activity of a waste automotive catalyst for methanol combustion increased after acid treatment. The acid effect of catalytic activity was summarized as follows: HNO3>HCI>H2SO4>CH3COOH. The waste automotive catalyst regenerated by the pretreatment method might have a excellent catalytic activity for VOCs combustion.

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전자빔으로 처리한 폐면의 버섯배지효과 (Utilization of Electron Beam-Radiated Cotton Waste for Agaric Mushroom Cultivation Bed)

  • 손효정;정선영;이종신;서영범
    • 펄프종이기술
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    • 제41권3호
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    • pp.71-75
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    • 2009
  • Cotton waste is usually used for cultivating agaric mushroom after outdoor fermentation for a few months. Electron beam was used to break down the polymer chaims of cotton waste for increasing low molecular weight soluble sugars, which may enhance the agaric mushroom cultivation. By increasing electron beam radiation, alpha cellulose content of the cotton waste was decreased while beta cellulose content and hot water solubles were increased. Electron beam radiation over 240 kGy on cotton waste caused significant increase of mushroom yield without lowering mushroom quality.

다중 고체상을 고려한 소결기의 코크스 연소-열전달 모델링 (Modeling of Coke Combustion and Heat Transfer in an Iron Ore Sintering Bed with Considerations of Multiple Solid Phases)

  • 양원;류창국;최상민
    • 대한기계학회:학술대회논문집
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    • 대한기계학회 2003년도 추계학술대회
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    • pp.79-84
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    • 2003
  • In this study we propose an unsteady I-dimensional model of an iron ore sintering bed with multiple solid phases, which confers a phase on each solid material. This model contains coke combustion, limestone decomposition, gaseous reaction, heat transfers between each phase, and geometric changes of the solid particles. Simulation results are compared with the limited experimental data set of various coke contents and air supply rates. Effect of the coke diameter is also evaluated. They predict the experimental results well and show applicabilities to the various system of the fuel bed with various solid materials.

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연도가스 열회수용 다관형 순환유동층 열교환기 성능실험 (Performance Test of a Multi-riser Fluidized Bed Heat Exchanger for Flue Gas Heat Recovery)

  • 전용두;이금배
    • 설비공학논문집
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    • 제16권3호
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    • pp.273-279
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    • 2004
  • A lab-scale fluidized bed heat exchanger for waste gas heat recovery is devised and tested. Compared to our previous works on fluidized bed type system with a single riser, the present heat exchanger system is featured by its multiple (four) risers to handle increased amount of exhaust gas. Particles are introduced to the main hot gas stream alongside the pipe circumference near riser inlets. The heat exchanger performance and pressure drop are evaluated through experiments for the present gas-to-water heat exchanger system.