• 제목/요약/키워드: $H_2S$ removal

검색결과 779건 처리시간 0.027초

식물성 식용유 첨가가 PAHs 오염토양 펜톤처리에 미치는 영향 (Effect of Vegetable Oils Addition on Fenton Treatment of PAHs-Contaminated Soil)

  • 강명화;김승호;박영구;박준석
    • 유기물자원화
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    • 제14권1호
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    • pp.160-168
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    • 2006
  • 본 연구에서는 PAHs 오염토양의 펜톤처리시 식물성 식용유와 폐식용유의 첨가가 처리효율에 미치는 영향을 알아보고자 실시하였다. 토양 중 철성분 때문에 철용액을 첨가하지 않고 과산화수소만을 첨가한 경우에도 펜톤반응이 진행되었으며, 과산화수소는 3%에서 최대 효율을 나타내었다. 3%의 과산화수소만을 첨가한 경우에는 총 PAHs가 약 19% 제거되었는데 여기에 17.5 mM $FeSO_4$(III)를 첨가한 경우에는 25%가 제거되어 6% 정도의 효율증진을 나타내었다. 올리브유 1%를 펜톤반응과 동시 또는 전에 첨가한 경우 제거효율은 37~38%로써 펜톤처리만을 한 경우의 22.3% 보다 약 15%정도 제거효율을 증가시킬 수 있었다. 올리브유, 콩식용유, 그리고 폐식용유 농도를 1%와 5%로 하여 주입한 결과 대부분 35% 이상의 처리효율을 나타내었으며, 오일의 종류와 농도에 따른 영향은 크지 않았다. 폐식용유를 사용하였을 때 고가의 올리브유를 사용한 경우와 큰 효율차이를 나타내지 않았으므로 폐식용유 사용시 추가비용이 거의 소요되지 않는 장점이 있을 것으로 판단된다. 3% 과산화수소와 2.5 mM $FeSO_4$에서 1% 올리브유 첨가 후 15분이 지나서 펜톤반응을 실시한 경우 벤젠고리 3~4개와 5~6개인 화합물의 제거율은 펜톤반응만을 실시한 경우 보다 각각 13%와 17% 정도 증가하였다.

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生物膜 電極反應機를 이용한 廚房廢水 처리 효과 (Effects of Domestic Wastewater Treatment used Biofilm-Electrode Reactor(BER))

  • Noh, Hyun-Woong;Yoon, Oh-Sub
    • 한국환경보건학회지
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    • 제23권1호
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    • pp.43-49
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    • 1997
  • This study was aimed to estimate removal efficiency(%) of BER(Biofilm-Electrode Reactor) and A.S(Activated Sludge) treatments. When were analyzed COD$_{Cr}$, NH$_3$-N and T-P by current density and reaction time, the results were as follows : 1) In BER treatment, the removal efficiency of COD$_{Cr}$ in domestic wastewater was 79-86% when current density was 2.39 mA/dm$2$(15mA)-3.98 mA/dm$^2$(25mA) and reaction time was 48 hr. 2) Removal efficiency of NH$_3$-N was 71-73% when current density was 2.39-3.98 mA/dm$^2$ and reaction time 48 hr. 3) When the reaction time was 48 hr removal efficiency(%) of BER treatment for COD$_{Cr}$, NH$_3$-N and T-P were more excellent than A.S. treatment. And then we prospect that was because activated microorganism colonies attached in biofilm on surface of electrode pannel. Therefore, In order to derive BER treatment efficiency(%) should establish optimum conditions of pH, temp., reaction time, current density and biochemical and electrochemical states.

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돈분뇨슬러리 폭기시 담체 설치효과 (The Effect of Media Application in Aeration Tank for Aerobic Treatment of Swine Slurry)

  • 정광화;조승희;곽정훈;김재환;정의수;정만순;강희설
    • 한국축산시설환경학회지
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    • 제16권3호
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    • pp.167-174
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    • 2010
  • 본 시험은 돈분뇨 슬러리�l 액상처리효과를 증시키기 위하여 담체를 활용한 폭기조 운영조건 변화에 따른 처리효과를 측정하기 위한 목적으로 수행하였으며, 시험 결과는 다음과 같다. 1. BOD와 COD의 제거효율은 일반 관행폭기에 비해 담체 처리구에서 더 좋은 결과를 보였다. 담체 중에서도 섬유상 담체에서 그 제거율이 높았다. SS의 경우는 관행 폭기처리구보다 담체 적용구에서 그 변화정도가 적었다. 반면에 질소의 제거율은 담체 적용에 의해 뚜렷하게 개선되었다. 2. 슬러지 침강성과 농축성을 나타내는 SVI 값은 대조구에서 나타난 25%에 비해 담체 적용구가 높았으며 섬유상 담체적용구에서 45%의 가장 높은 감소정도를 보였다. 3. 관행 폭기구에서의 슬러지 발생량을 100으로 기준하여 볼 때 섬유담체에서 약 85% 정도의 슬러지 발생량을 보임으로써 각 처리구중에서 슬러지 발생량이 가장 적은 것으로 나타났다. 4. 담체를 적용한 경우 슬러지중의 휘발성 고형분 함량이 일반 관행 폭기구에서 발생한 슬러지보다 더 낮아지는 결과를 보였다.

아연-티타늄 복합산화물 탈황제의 제조 및 반응특성 연구 (A Study on Preparation and Reactivity of Zinc Titanate Sorbents for H2S Removal)

  • 김기석;박노국;이태진
    • 공업화학
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    • 제8권1호
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    • pp.122-131
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    • 1997
  • 아연-티타늄 복합금속산화물 탈황제를 제조하여 석탄가스중의 $H_2S$를 제거하는 고온탈황성능을 연구하였다. $H_2S$ 흡수에 의한 탈황제의 황화반응실험을 충전층 관형 흐름반응기를 사용하여 $550{\sim}750^{\circ}C$ 범위에서 수행한 결과 탈황율과 아연성분의 손실측면에서 $650^{\circ}C$가 최적 황화반응 온도임이 밝혀졌다. SEM 분석에 의해서 $650^{\circ}C$에서의 황화반응과 $750^{\circ}C$에서의 재생반응에 따른 탈황제 입자의 구조변화를 관찰하였다. 탈황성능의 지속성과 탈황제 내구성을 평가하기 위하여 연속적인 황화-재생 cycle 반응실험을 수행하였으며 10번째 cycle 이후에 수거반 탈황제 시료의 특성을 BET, XRD, SEM/EDX에 의해서 분석하였다. 아연-티타늄 복합 산화물 탈황제는 연속적인 황화-재생 cycle 동안에 거의 일정한 탈황성능을 나타내었다.

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폐주물사를 이요한 인제거 (The Removal of Phosphorus by Spent Foundry Sand)

  • 윤철종;진양오;박승조
    • 자원리싸이클링
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    • 제8권3호
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    • pp.26-30
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    • 1999
  • 폐주물사 재이용 방안으로 하수처리시 폐주물사를 여재로써 이용하여 인제거에 적용하고져 하였다. 용액의 pH를 2, 6, 11로 조정하여 인제거 실험한 결과 pH2에서 가장 우수한 제거율을 나타내었으며 폐주물산 100g 으로 반응시켰을 경우 2시간의 반응에서 99.9% 이상의 인제거율은 나타내었다. 또한 Langmuir 등온 흡착 모델에 적용한 결과 ${\Gamma}=0.0005{\theta}$/(1+2.4987 $\theta$)의 등온흡착식을 얻었으며 연속식 실험에서 파괴농도를 8mg/l로 하였을 경우 폐주물사의 파과시산은 25hrs으로 나타났다.

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The utilization of waste seashell for high temperature desulfurization

  • Kim, Young-Sik;Kim, Taek-Geun;Sim, Eon-Bong;Seo, Jeong-Min
    • 한국환경보건학회:학술대회논문집
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    • 한국환경보건학회 2005년도 Proceedings of KSEH.Minamata Forum
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    • pp.66-71
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    • 2005
  • The waste seashells were used for the removal of hydrogen sulfide from a hot gas stream. The sulphidation of waste seashells with $H_2S$ was studied in a thermogravimetric analyzer at temperature between 600 and 800$^{\circ}C$. The desulfurization performance of the waste seashell sorbents was experimentally tested in a fixed bed reactor system. Sulfidation experiments performed under reaction conditions similar to those at the exit of a coal gasifier showed that preparation procedure and technique, the type and the amount of seashell, and the size of the seashell affect the $H_2S$ removal capacity of the sorbents. The pore structure of fresh and sulfided seashell sorbents was analyzed using mercury porosimetry, nitrogen adsorption, and scanning electron microscopy.

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악취 발산감소를 위한 필터의 이용 효과 (Effect of Biofilter on Reducing Malodor Emission)

  • 김원영;정광화;노진식;김원호;전병수;류호현;전영륜
    • 한국축산시설환경학회지
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    • 제4권2호
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    • pp.161-166
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    • 1998
  • Controlling malodor originating from livestock feces has become a major issue, due to its influence on the health of man and livestock, together with its influences on atmospheric pollution. In this study, Five types of biofilters filled with saw-dust, night soil, fermented compost, leaf mold and a mixture(a compound of night soil, fermented compost and leaf mold at the same rates, respectively) were manufactured and tested. To study the effect of the biofilter on reducing malodor in a composting facility and swine building, a pilot scale composting facility enclosed with polyethylene film was constructed. Swine feces was composted in the facility and malodorous gas generated from the decomposition of organic matter in the feces was gathered by vacuum pump. Each biofilter achieved 87∼96% NH3 removal efficiency. This performance was maintained throughout 10 days of operation. The highest NH3 removal efficiency was achieved by leaf mold on the first day of operation period. It reduced the concentration of NH3 by about 96%. Night soil and fermented compost showed nearly equal performance of 93 to 94% for 10 days from the beginning of operation. The mixture achieved the lowest NH3 removal efficiency. It reduced NH3 concentration by about 89∼94% for 10 days from the beginning of operation. However NH3 removal efficiency of each biofilter declined with the passage of operational time. After 30 days from the beginning of operation, NH3 removal efficiency of each biofilter of each biofilter was below 60%, respectively. The concentration of H2S and CH3-SH originating from compost were equal to or less than 5mg/l and 3mg/l, respectively. After passing throughout the biofilter, the concentration of H2S and CH3-SH were not detected.

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황화수소 제거를 위한 칼슘계 고온탈황제의 황화반응속도에 관한 연구 (Kinetic study of high-temperature removal of $H_2S$ by Ca-based sorbents)

  • 김영식;전지환
    • 한국환경과학회:학술대회논문집
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    • 한국환경과학회 1998년도 봄 학술발표회 프로그램
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    • pp.144-153
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    • 1998
  • Sorbents of calcined limestone and oyster particles having a diameter of about 0.63mm were exposed to simulate fuel gases containing 5000ppmv H2S for temperatures ranging from 600 to 800C in a TGA. The reaction between CaO and H2S proceds via an unreacted shrinking core mechanism. The sulfidation rate is likely to be controlled primarily by countercurrent diffusion through the product layer of calcium sulfide(CaS) formed. The kinetics of the sorption of H2S by CaO is sensitive to the reaction temperature and particle size, and the reaction rate of oyster was faster than the calcined limestone.

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황화수소 제거를 위한 칼슘계 고온 탈황제의 황화반응속도 (Kinetic of High-Temperature Removal of $H_2S$ by Ca-based Sorbents)

  • 김영식;전지환;손병현;정종현;정덕영;오광중
    • 한국환경과학회지
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    • 제8권1호
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    • pp.125-133
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    • 1999
  • Sorbents of calcined limestone and oyster particles having a diameter of about 0.63mm were exposed to simulated fuel gases containing 5000ppm $H_2S$ for temperatures ranging from 600 to 80$0^{\circ}C$ in a TGA (Thermalgravimetric analyzer). The reaction between CaO and $H_2S$ proceeds via an unreacted shrinking core mechanism. The sulfidation rate is likely to be controlled primarily by countercurrent diffusion through the product layer of calcium sulfide(CaS) formed. The kinetics of the sorption of $H_2S$ by CaO is sensitive to the reaction temperature and particle size, and the reaction rate of oyster was faster than the calcined limestone.

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Porosity and Liquid-phase Adsorption Characteristics of Activated Carbons Prepared From Peach Stones by $H_3PO_4$

  • Attia, Amina A.;Girgis, Badie S.;Tawfik, Nady A.F.
    • Carbon letters
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    • 제6권2호
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    • pp.89-95
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    • 2005
  • Crushed peach stone shells were impregnated with $H_3PO_4$ of increasing concentrations (30-70%) followed by heat treatment at 773 K for 3 h. Produced carbons (ACs) were characterized by $N_2$ adsorption at 77 K using the BET-equation and the ${\alpha}$-method. High surface area microporous ACs were obtained, with enhanced internal pore volume, as function of % $H_3PO_4$. Adsorption isotherms from aqueous solution were determined for methylene blue (MB) and p-nitrophenol (PNP), as representatives for dye and phenolics pollutant molecules. Application of the Langmuir model proved the high limiting capacity towards both solute molecules, MB was uptaken in increasing amounts as function of $H_3PO_4$ concentration and generated porosity. High removal of PNP was almost the same irrespective of porosity characteristics. Competitive adsorption of $H_2O$ molecules on the hydrophilic carbon surface seems to partially reduce the available area to the PNP molecules. Application of the pseudo-second order law described well the fast adsorption (${\leq}$ 120 min) at two initial dye concentrations.

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