• 제목/요약/키워드: $SO_2$ Removal

검색결과 1,088건 처리시간 0.031초

건식 FGD 공정에서 SO2 제거를 위한 Ca(OH)2 및 CaCO3 원료의 다공성 필터 제조 및 특성 (Preparation and Characterization of Porous Filters from Ca(OH)2 and CaCO3 for SO2 Removal in Dry-FGD Process)

  • 한요섭;김현중;박영구;박재구
    • 공업화학
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    • 제16권6호
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    • pp.772-777
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    • 2005
  • 본 연구에서는 발포법 및 겔-캐스팅법을 이용하여 소석회와 석회석을 원료로 다공성 필터의 제조를 제조하였다. 제조된 필터의 물성과 $SO_2$ 제거성능을 평가한 결과 다공성 석회질 필터의 기공률 및 기공크기가 클수록 수많은 윈도우에 의해서 대부분의 기공이 열린 기공으로 형성됨을 알 수 있었다. $SO_2$ 제거에 대한 다공성 석회질 필터의 영향은 다음과 같이 관찰되었다. 반응온도가 증가할수록 $SO_2$ 제거효율은 증가하였다. $SO_2$ 유입농도에 따른 제거 효율의 차이가 많이 나지 않았지만 유량 차이에 의한 효율 변화는 상대적으로 크게 나타났다. 필터의 경우 기공률이 클수록 $SO_2$ 제거효율은 우수하였으며, 기공률이 동일한 경우에서는 소석회 필터는 석회석 필터보다 $SO_2$ 제거효율이 우수하였다. 이것은 소석회의 CaO 전환율이 석회석에 비해 우수하여 $SO_2$에 의해 상대적으로 쉽게 $CaSO_4$로 형성되었기 때문으로 판단된다.

중소형 선박의 $SO_X/NO_X$ 동시제거를 위한 습식세정시스템 (Simultaneous removal of $SO_X$ and $NO_X$ by wet scrubber at small and medium craft)

  • 차유정;이주열;하태영;박병현
    • 한국응용과학기술학회지
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    • 제31권1호
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    • pp.159-166
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    • 2014
  • In recent years, researchers have put a considerable effort to decrease the emission of harmful gaseous pollutants to the atmosphere. In order to remove simultaneously $SO_2$ and $NO_X$ from the flue gas of small and medium-sized ship, we designed minimal wet scrubber inside a compact multistage modular system. In this study we proceed experiment of elemental technology at each stage of the scrubber. The each stage is oxidation of NO which is the main component of $NO_X$, and removal of $SO_2$, respectively. $NaClO_2$ was used to oxidize NO gas, and NaOH was used to remove $SO_2$ gas. The maximum NO conversion efficiency and the $SO_2$ removal efficiency are both indicate 100%.

건식세정기에서의 오염물 동시제거를 위한 고온3계평형 모델의 적용과 예비설계에의 응용 (Application of High-temperature 3-phase Equilibrium Distribution to Dry Scrubber for the Simultaneous Removal of $SO_2$ and Vinyl Chloride)

  • 구자공;백경렬
    • 한국대기환경학회지
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    • 제6권1호
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    • pp.85-96
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    • 1990
  • Simultaneous removal efficiencies of hydrophilic and hydrophobic gaseous pollutants are experimentally determined, and the macroscopic removal mechanism of pollutants in a dry scrubber is analyzed using the extended model of three phase equilibrium distribution of pollutant at high temperatures that can describe the different morphological conditions of adsorbent and water at varying relative humidities. For the simplicity, the inside of spray dryer is divided into three regions of ; (1) absorption, (2) three-phase equilibrium, and (3) adsorption, and the removal efficiencies of each pollutants at three regions are observed at different experimental conditions to estimate the effects of important parameters of dry scrubber. The laboratory experiments simulate the three regions of spray dryer with the temperature control and thus evaporation rate of water from the slurry particle. $SO_2$ as a hydrophilic gaseous pollutant and vinyl chloride as a hydrophobic toxic gas are selected for the future field application to soid waste incineration, and the two types of slurry are made of the two sorbents ; 10 wt.% $Ca(OH)_2$, and 10 wt.% NaOH. Result of temperature effect shows the height of absorption plus three-phase region is decreased as the operation temperature is increased, which results in the lower removal efficiency of $SO_2$ but higher removal for vinyl chloride in the adsorption region of dry scrubber. The removal efficiency of $SO_2$ is higher by NaOH slurry than by $Ca(OH)_2$ slurry due to the hygroscopic nature of NaOH, while the removal of vinyl chloride is higher in $Ca(OH)_2$ case. From the analysis of redults using three-phase equilibrium distribution model, the effective two-phase partition coefficients can be obtained, and the possible extention in the application of the three-phase equilibrium model in a dry scrubber design has been demonstrated.

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알루미나에 의한 수용액 중의 산성이온 제거 특성 (Removal Characteristic of Acidic Ion in Aqueous Solution by Alumina)

  • 홍영호
    • 공업화학
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    • 제18권5호
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    • pp.454-458
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    • 2007
  • 본 연구는 알루미나를 이용하여 수용액 중에 존재하는 $Ca^{2+}$, $Mg^{2+}$, $Sr^{2+}$, $SO{_4}^{2-}$, $NO{_3}^-$, $Cl^-$ 이온의 제거 특성을 분석하기 위하여 실시하였다. 알루미나는 $Al(NO_3)_3{\cdot}9H_2O$$NH_4OH$를 사용하여 합성한 수화물을 $450{\sim}750^{\circ}C$로 5 h 동안 열처리하고 FT-IR과 Brunauer-Emmett-Teller (BET)법으로 물성을 분석하였다. 실험결과에 의하면 알루미나의 비표면적은 열처리 온도가 증가하면 감소하는 특성을 나타내었다. 알루미나에 의한 흡착능은 $SO{_4}^{2-}$$NO{_3}^-$가 각각 23 mg/g와 12.4 mg/g의 값을 보였다. 반면에 $Cl^-$는 4 mg/g으로 비교적 낮은 값을 보였다. 일반적으로 음이온 제거 효율은 알루미나의 제조를 위한 열처리 온도가 증가할수록 감소하였으며, $450^{\circ}C$로 처리한 알루미나의 경우에 가장 좋은 처리 효율을 나타내었다. 양이온인 $Ca^{2+}$, $Mg^{2+}$, $Sr^{2+}$의 제거 효율은 알루미나의 열처리 온도에 비례하여 증가하는 경향을 보였다.

전기투석을 이용한 지하수 중의 질산성질소 제거 (The removal of Nitrate-nitrogen from ground water by electrodialysis)

  • 민지희;김한승
    • 상하수도학회지
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    • 제22권3호
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    • pp.307-314
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    • 2008
  • In this study, the effects of applied voltage, solution pH and coexistence of other ions such as sulfate ion (${SO_4}^{2-}$) and chloride ion ($Cl^-$) were investigated on the removal of nitrate-nitrogen ($NO_3{^-}-N$) from ground water by electrodialysis. The examined operating conditions were evaluated for optimizing the removal efficiency of $NO_3{^-}-N$. Real ground water samples taken from a rural area of Yongin city and artificial ones with components similar to the real ground water were tested for the study, which contained $NO_3{^-}-N$ concentration of 17mg/L that exceeds current drinking water quality standard of 10 mg/L. The increase in the removal rate of $NO_3{^-}-N$ was observed as the applied voltage increased from 5V to 30V, while no significant increase in the removal rate appeared at the applied voltage beyond 20V during a given operating time. The removal rate appeared to get lower at both acidic and basic condition, compared to neutral pH. Coexistence of of ${SO_4}^{2-}$and $Cl^-$ demanded much longer operating time to achieve a given removal rate or to meet a certain level of treated water concentration. When nitrate ion was combined with ${SO_4}^{2-}$and $Cl^-$, the removal rate was reduced by 4.29% and 10.83%, respectively.

SPCP를 이용한 오염물질 ($SO_2$, NOx) 처리 특성 (The Characteristics of the Treatment of Pollutants ($SO_2$, NOx) Using Surface Discharge Induced Plasma Chemical Process)

  • 봉춘근;부문자
    • 한국대기환경학회지
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    • 제14권4호
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    • pp.333-342
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    • 1998
  • Plasma process has great possibilities to remove SOx, NOx simultaneously with high treatment efficiency and is expected to be suitable for small or middle plants. It was accomplished to evaluate SO2, NOx control possibility and achieve basic data to control pollutants by use of Surface Discharge Induced Plasma Chemical Process (SPCP) in this study. O3 generation characteristics by discharge of a plate was proportional to O2 concentration and power consumption and inversely proportional to temperature and humidity, In case of dry air, NOx was highly generated by N2 and O2 in air during the plasma discharge process but it was decreased considerably as H2O was added. SO2 removal efficiency was very high, and removal rate was 170,350 mEA at 30,50 watt respectively in flue gas which is usually contain HIO. NOx removal efficiency was about 57% at 40 watt power consumption with 7.5% humidity. It is estimated that H2O has an important role in reaction mechanism with pollutants according to plasma discharge.

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도금폐수내 유리시안과 착염시안 및 중금속의 처리특성 (I) (Treatment Characteristics of Plating Wastewater Containing Freecyanide, Cyanide Complexes and Heavy Metals (I))

  • 정연훈;이수구
    • 한국물환경학회지
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    • 제25권6호
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    • pp.979-983
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    • 2009
  • The mean pH of wastewater discharged from the plating process is 2, so a less amount of alkali is required to raise pH 2 to 5. In addition, if sodium sulfite is used to raise pH 5 to 9 in the secondary treatment, caustic soda or slaked lime is not necessary or only a small amount is necessary because sodium sulfite is alkali. Thus, it is considered desirable to use only $FeSO_4{\cdot}7H_2O$ in the primary treatment. At that time, the free cyanide removal rate was highest as around 99.3%, and among heavy metals, Ni showed the highest removal rate as around 92%, but zinc and chrome showed a low removal rate. In addition, the optimal amount of $FeSO_4{\cdot}7H_2O$ was 0.3g/L, at which the cyanide removal rate was highest. Besides, the free cyanide removal rate was highest when pH value was 5. Of cyanide removed in the primary treatment, the largest part was removed through the precipitation of ferric ferrocyanide: $[Fe_4(Fe(CN)_6]_3$, and the rest was precipitated and removed through the production of $Cu_2[Fe(CN)_6]$, $Ni_2[Fe(CN)_6]$, CuCN, etc. Furthermore, it appeared more effective in removing residual cyanide in wastewater to mix $Na_2SO_3$ and $Na_2S_2O_5$ at an optimal ratio and put the mixture than to put them separately, and the optimal weight ratio of $Na_2SO_3$ to $Na_2S_2O_5$ was 1:2, at which the oxidative decomposition of residual cyanide was the most active. However, further research is required on the simultaneous removal of heavy metals such as chrome and zinc.

SO2 제거를 위한 중공사막 기-액 접촉기의 모사 및 분리막 물질 전달 계수 추정 (The Computer Simulation and Estimation of Membrane Mass Transfer Coefficients of Hollow Fiber Membrane G-L Contactors for SO2 Removal)

  • 김용국;송희열;이형근;김인원
    • Korean Chemical Engineering Research
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    • 제45권1호
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    • pp.81-86
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    • 2007
  • 산업 시설에서 발생하는 $SO_2$를 제거하기 위해 중공사막 기-액 접촉기를 사용하고 있다. 본 연구에서는 기-액 접촉기 내의 중공사막에서의 $SO_2$ 흡수거동 대하여 수학적으로 모델링하고, 그 모델을 유한 요소 분석법을 이용하여 모사하였다. $SO_2$의 분리에 영향을 주는 변수인 기체 유량, 분리막의 물질 전달 계수 및 접촉기의 물리적 특성에 따른 $SO_2$의 분리 효율 및 물질 전달 특성을 알아보았다. 기체의 유속 변화에 따른 중공사막을 통한 $SO_2$ 제거 효율 실험값으로부터 분리막의 물질 전달 계수를 추정하였다. 또한 중공사막 설계에 도움이 되는 자료를 계산할 수 있는 방법을 제시하였다.

촉매 담지 코디어라이트 다공성 필터의 NOx/SOx 동시제거에 대한 연구 (Simultaneous Removal of NOx/SOx by Catalyst-loaded Cordierite Porous Filter)

  • 이시희;정구춘;김지웅;신민철;이희수
    • 분석과학
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    • 제15권3호
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    • pp.256-262
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    • 2002
  • 평균입자크기가 200 ${\mu}m$인 코디어라이트 분말을 사용하여 다공성 필터를 제조한 후, 진공함침법으로 $V_2O_5$, CuO, $LaCoO_3$ 촉매를 담지시킨 후 NO와 $SO_2$ 기체를 촉매 담지 세라믹필터에 동시 통과시키면서 NOx/SOx의 동시제거효율을 측정하였다. 제조된 다공성 필터의 기공률은 61.6%였고, 압축강도는 12.3 MPa이었으며, 면속도 5 cm/sec에서의 차압은 147 Pa이었다. NO와 $SO_2$의 동시제거효율을 분석해 본 결과, 페로브스카이트계 $LaCoO_3$ 촉매의 동시제거효율이 가장 우수함을 확인하였으며, $LaCoO_3$ 촉매의 NO에 대한 제거효율은 90% 이상, $SO_2$에 대해서는 80% 이상이었다.

석회질 다공성 필터 제조 및 SOx 제거 특성 (Preparation of Porous Lime Filters and SOx Removal Characteristics)

  • 이광희;박재구;김현중
    • 한국대기환경학회지
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    • 제20권2호
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    • pp.153-159
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    • 2004
  • This study was focused on evaluating physical properties and SO$_{x}$ removal capability of porous lime filters prepared by a foaming and a gelcasting method. Porosities of lime filters ranged from 55% to 85%, and their mean pore sizes were about 95 ${\mu}{\textrm}{m}$. It was observed that porous lime filters had the continuous pore structure that most pores were inter-connected by many windows. Before SO$_{x}$ removal reaction a surface of porous lime filters was made up of calcium oxide, but after reaction calcium sulfate became a main component. The SO$_{x}$ removal efficiency and the conversion ratio of calcium oxide to calcium sulfate increased according to reaction temperature and porosity. At 100$0^{\circ}C$, SO$_{x}$ removal efficiency of filters was always over 98% regardless of the porosity. In case of the filter with the porosity of 85%, the conversion ratios of calcium oxide increased according to the reaction temperature, and they were in the range 30% to 60%. to 60%.