• 제목/요약/키워드: Arsenic(V) adsorption

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나노 크기 적철석 입자 피복 모래를 이용한 지하수내 비소 3가와 5가의 제거 기술 개발

  • 고일원;이철효;이상우;김주용;김경웅
    • 한국지하수토양환경학회:학술대회논문집
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    • 한국지하수토양환경학회 2003년도 추계학술발표회
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    • pp.78-82
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    • 2003
  • Development of hematite-coated sand was evaluated for the application of the PRB (permeable reactive barrier) in the arsenic-contaminated subsurface of the metal mining areas. The removal efficiency of As(III) and As(V), the effect of anion competition and the capability of arsenic removal in the flow system were investigated through the experiments of adsorption isotherm, arsenic removal kinetics against anion competition and column removal. Hematite-coated sand followed a linear adsorption isotherm with high adsorption capacity at low level concentrations of arsenic (< 1.0 mg/l). When As(III) and As(V) underwent adsorption reactions in the presence of anions (sulfate, nitrate and bicarbonate), sulfate caused strong inhibition of arsenic removal, and bicarbonate and nitrate caused weak inhibition due to specific and nonspecific adsorption onto hematite, respectively. In the column experiments, high content of hematite-coated sand enhance the arsenic removal, but the amount of the arsenic removal decreased due to the higher affinity of As(V) than As(III) and reduced adsorption kinetics in the flow system, Therefore, the amount of hematite-coated sand, the adsorption affinity of arsenic species and removal kinetics determined the removal efficiency of arsenic in the flow system. arsenic, hematite-coated sand, permeable reactive barrier, anion competition, adsorption.

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Iron Mixed Ceramic Pellet for Arsenic Removal from Groundwater

  • Shafiquzzam, Md.;Hasan, Md. Mahmudul;Nakajima, Jun
    • Environmental Engineering Research
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    • 제18권3호
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    • pp.163-168
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    • 2013
  • In this study, an innovative media, iron mixed ceramic pellet (IMCP) has been developed for arsenic (As) removal from groundwater. A porous, solid-phase IMCP (2-3 mm) was manufactured by combining clay soil, rice bran, and Fe(0) powder at $600^{\circ}C$. Both the As(III) and As(V) adsorption characteristics of IMCP were studied in several batch experiments. Structural analysis of the IMCP was conducted using X-ray absorption fine structure (XAFS) analysis to understand the mechanism of As removal. The adsorption of As was found to be dependent on pH, and exhibited strong adsorption of both As(III) and As(V) at pH 5-7. The adsorption process was described to follow a pseudo-second-order reaction, and the adsorption rate of As(V) was greater than that of As(III). The adsorption data were fit well with both Freundlich and Langmuir isotherm models. The maximum adsorption capacities of As(III) and As(V) from the Langmuir isotherm were found to be 4.0 and 4.5 mg/g, respectively. Phosphorus in the water had an adverse effect on both As(III) and As(V) adsorption. Scanning electron microscopy results revealed that iron(III) oxides/hydroxides are aggregated on the surface of IMCP. XAFS analysis showed a partial oxidation of As(III) and adsorption of As(V) onto the iron oxide in the IMCP.

칼럼을 이용한 토양에서 As(III)와 As(V)의 흡착 및 탈착에 관한 연구 (A Study on Adsorption and Desorption of As(III) and As(V) on Soil using a Column)

  • 김명진;김태석
    • 한국지하수토양환경학회지:지하수토양환경
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    • 제13권1호
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    • pp.52-59
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    • 2008
  • 흡착은 비소가 토양에 축적되는 주요 과정이다. 그러므로 토양에서 비소종의 흡착 및 탈착 특성을 이해하는 것은 비소종의 거동을 예측하고 토양으로부터 비소를 제거하는 적절한 정화방법을 수립하기 위해 필수적이다. 본 연구에서는 칼럼을 이용하여 토양에서 As(III)와 As(V)의 흡착 및 탈착실험을 수행하였다. As(III)에 대한 실험은 환원환경에서, 그리고 As(V)에 대한 실험은 산화환경에서 실시했다. 실험이 진행되는 동안 대부분의 As(III)는 그 산화상태를 유지하였다. As(III)의 흡착 및 탈착속도는 As(V)보다 빨랐다. 칼럼실험에서 비소종의 흡착 및 탈착반응은 완전히 가역적은 아니었다. 또한 As(V)는 회분식실험에서보다 칼럼실험에서 더 빠르게 토양에 흡착되었다.

Removal of Arsenic(V) from Aqueous Solutions by Using Natural Minerals

  • Mohapatra Debasish;Mishra Debaraj;Chaudhury G. Roy;Das R.P.;Park, Kyung-Ho
    • 자원리싸이클링
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    • 제15권5호
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    • pp.38-46
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    • 2006
  • The removal of arsenic(V) using four different natural minerals were evaluated. Parameters like contact time, pH, adsorbent dosages, and As(V) concentration were optimized. The kinetics of adsorption was observed to be fast and reached equilibrium within 2h. As(V) adsorption on studied minerals was dependent on pH and followed a pseudo-second-order reaction model. For kaolin, maximum adsorption was found at pH 5.0. Whereas, in case of other three minerals, a pH range of 6.0-7.0 was found to be the best for As(V) adsorption. The maximum adsorption capacity (Q) was calculated by fitting Langmuir equation to the adsorption isotherms obtained under a specified condition. From the slope of best fit, the Q values were calculated to be 2.07, 2.15, 1.95 and 0.86 mg As(V)/g of bauxite, wad, iron ore and kaolin, respectively. Desorption of As(V) from loaded materials was dependent on the type of leaching reagents used. Based on the results, it was found that among the studied natural minerals, wad was the best As(V) adsorbent.

재생 알루미늄 산화물을 이용한 비소 흡착 특성 (Adsorption Characteristics of Arsenic using the Recycled Aluminium Oxide)

  • 민경철;김원기;이승목;김근한;이희용;양재규;박연종
    • 한국물환경학회지
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    • 제27권4호
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    • pp.486-490
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    • 2011
  • As(V) adsorption on aluminum oxide powder which was recycled from industrial wastes containing aluminum hydroxide was evaluated. Aluminum oxide powder in this study was prepared by calcinating aluminum hydroxide wastes at$550^{\circ}C$. Spectroscopic analysis indicated that the aluminum hydroxide wastes were changed to aluminum oxide by calcination. Arsenic adsorption isotherm was conducted with variation of ionic strength and multiple-ion systems using Ca(II) and Cu(II). As(V) removal showed typical anionic adsorption characteristics that the removal efficiency decreased with increasing pH in single As(V) system as well as in binary and ternary system. More than 80% of As(V) at an initial concentration of $5{\times}10^{-5}$ M was removed from aluminum oxide powder in As(V) single system. The effect of ionic strength on As(V) adsorption was negligible, which indicated the strong bonding between aluminum oxide powder and As(V). The removal efficiency of As(V) was higher in a binary system with Cu(II) than in a binary system with Ca(II).

비소의 적철석 표면 흡착에 토양유기물이 미치는 영향: 화학종 모델링과 흡착 기작 (Effect of Soil Organic Matter on Arsenic Adsorption in the Hematite-Water Interface: Chemical Speciation Modeling and Adsorption Mechanism)

  • 고일원;김주용;김경웅;안주성
    • 자원환경지질
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    • 제38권1호
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    • pp.23-31
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    • 2005
  • 본 연구는 이성분계의 화학종 모델링과 삼성분계의 흡착 모델링으로부터 As(III)와 As(V)의 적철석 표면 흡착에 휴 믹산의 영향과 그 결합기작을 고찰하였다. 비소와 휴믹산의 유기 결합의 모델링은 음이온 사이의 정전기적인 반발력 과 비소의 유기 결합을 위한 결합금속의 영향을 고려한 결합 모델이 적합하였다. 삼성분계의 흡착 실험 자료와 비교 할 때 이성분계의 고유상수를 사용한 음이온 경쟁 모델이 음이온 경쟁에 따른 비소의 흡착량과 일치하였다. 반면, 비 소의 유기 결합량의 감소와 휴믹산과의 음이온 흡착경쟁이 흡착량을 감소시키기 때문에 단순합모델은 양이온 중금속 과는 반대로 모델의 편차를 보였다. 반응 기작의 관점에서 휴믹산의 공존하에 비소 유기결합 화학종과 중성화학종의 As(III) 및 음이온의 As(V)가 속착물을 형성하며, 경쟁적으로 적철석 표면으로 이동하여 흡착하게 된다.

재생 알루미늄 산화물과 $TiO_2$의 복합성형체를 이용한 비소 흡착 특성 (Adsorption Characteristics of Arsenic on Composite Adsorbents using Recycled Aluminium Oxides and $TiO_2$)

  • 민경철;이승목;김근한;이희용;양재규;박연종
    • 한국물환경학회지
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    • 제28권2호
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    • pp.197-201
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    • 2012
  • The objective of this study was to evaluate the removal efficiency of arsenite and arsenate using composite adsorbents with various mixing ratio of recycled aluminum oxides and $TiO_2$. From batch adsorption experiments, while the removal of As(III) was almost same with 4 different composite samples in the entire pH range, the removal of As(V) was substantially increased as the weight ratio of $TiO_2$ in composite samples reduced and showed anionic adsorption characteristics. Both adsorption of As (III) and As(V) on composite samples followed pseudo-second-order adsorption equation and C-3 showed faster reaction rate for the removal of arsenic. From the adsorption isotherm experiments, Langmuir isotherm explained well and the maximum adsorption capacities of arsenic were obtained with C-1.

Modeling As(III) and As(V) adsorption and transport from water by a sand coated with iron-oxide colloids

  • Ko, Il-Won;Lee, Cheol-Hyo;Kim, Kyoung-Woong
    • 한국지하수토양환경학회:학술대회논문집
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    • 한국지하수토양환경학회 2004년도 총회 및 춘계학술발표회
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    • pp.243-247
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    • 2004
  • Tile development of a porous iron-oxide coated sand filter system can be modelled with the analytical solution of tile transport equation in order to obtain the operating parameters and investigate the mechanism of arsenic removal. The adsorbed amount from the model simulation showed the limitation of adsorption removal during arsenic transport. A loss reaction term in the transport equation plays a role in the mass loss in column conditions, and then resulted into the better model fitting, particularly, for arsenate. Further, the competitive oxyanions delayed the breakthrough near MCL (10 $\mu$g/L) due to the competitive adsorption. This is the reason why arsenate can be strongly attracted in tile interface of an iron-oxide coated sand, and competing oxyanions can occupy the adsorption sites. Therefore, arsenic retention was regulated by non-equilibrium of arsenic adsorption in a porous iron-oxide coated sand media. The transport-limited process seemed to be affect the arsenic adsorption by coated sand.

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비소의 Two-Line Ferrihydrite에 대한 흡착반응 (Adsorption of Arsenic onto Two-Line Ferrihydrite)

  • 정영일;이우춘;조현구;윤성택;김순오
    • 한국광물학회지
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    • 제21권3호
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    • pp.227-237
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    • 2008
  • 최근 들어 비소오염에 대한 환경적 관심이 증대되면서, 세계적으로 비소에 대한 음용수 기준이 강화되고 있으며, 국내적으로도 비소로 오열된 지하수 덴 토양의 출현 빈도가 높아지면서 비소 오염과 그에 대한 처리 및 대책이 주요한 환경적 관심사로 대두되고 있다. 지중에서 비소의 거동은 주로 산화물들과 점토광물에 의하여 제어되는데, 특히 철(산)수산화물이 가장 효과적으로 비소를 제어하는 것으로 알려져 있다. 이에 본 연구에서는 다양한 철(산)수산화물들 중 2-line ferrihydrite가 비소의 거동에 어떠한 영향을 미치는가를 파악하기 위하여 수행되어졌다. 다양한 비소 화학종들 중 자연 상에서 발현 빈도수가 가장 큰 3가 비소(아비산염)와 5가 비소(비산염)가 2-line ferrihydritc와 어떠한 흡착 특성을 갖는지 비교하여 연구하였다. 비소의 흡착제로 실험실에서 제조되어 이용된 2-line ferrihydrite는 $10\sim200nm$의 작은 나노 크기, $247m^{2}/g$의 비교적 큰 비표면적, 다른 철(산)수산화물보다 높은 8.2의 영전하 pH 등을 갖는 것으로 나타났는데, 이러한 2-line ferrihydrite의 대표적인 물리화학적인 특성들은 비소의 흡착제로서 매우 적합한 것으로 조사되었다. 평형흡착 실험결과, 3가 비소가 5가 비소보다 월등히 높은 흡착력을 보였으며, 3가 비소는 pH 7.0, 5가 비소는 pH 2.0에서 가장 놀은 흡착력을 보이는 것으로 나타났다. 3가 비소는 pH 12.2를 제외하고는 pH에 따른 흡착량이 크게 차이를 보이지 않은 반면, 5가 비소는 pH가 증가함에 따라 흡착량이 현격하게 갈소하는 것으로 나타났다. pH에 따른 비소의 흡착특성을 보다 더 자세하게 초찰한 견과, 3가 비소는 pH 8.0까지는 흡착량이 증가하다가 pH 9.2 이상에서는 흡착량이 급격하게 같소하는 것으포 나타났다. 5가 비소의 경우에는 pH가 증가할 수록 비교적 일정하게 흡착량이 갉소하는 것을 알 수 있었다. 이렇게 비소 화학종에 따라서 상이한 흡착특성을 보이는 이유는 pH에 따른 각 비소 화학종의 화학져 존재 형태(chemical speciation)와 2-line ferrihydrite의 표면전하의 변화 등이 복합적으로 작용하기 때문인 것으로 사료된다. 각 비소 화학종과 2-line ferrihyite와의 흡착특성을 반응속도론적 관점에서 고찰한 결과, 대부분의 비소종들이 2시간 이내에 흡착이 거의 완료되는 것으로 나타났으며, 두 종류의 비소 화학종과 2-line ferrihydrite의 흡착 반응속도를 가장 잘 모사하는 반응속도 모댁은 power function과 elovich model인 것으로 조사되었다.

철산화물의 합성 및 이를 이용한 비소의 흡착제거 (Synthesis of Iron Oxide and Adsorption of Arsenic on Iron Oxide)

  • 김연정;최식영;김영훈
    • 한국환경과학회지
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    • 제28권1호
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    • pp.99-106
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    • 2019
  • Arsenic is among the heavy metals commonly found in aqueous environments. Iron oxide is known as an efficient adsorbent for the arsenic. A new synthetic method was applied to provide iron oxide giving a large specific surface area. The mixing method affects the formation of iron oxide. Ultrasonic waves assisted the formation of very fine iron oxide in an organic phase. The synthesized iron oxide is amorphous type with a high surface area of more than $181.3m^2/g$. Sorption capacity of the synthesized adsorbent was relatively very high for arsenic and varied depending on the oxidation state of arsenic: a higher capacity was obtained with As(V). Lower solution pH provided a higher sorption capacity for As(V). The competitive effect of co-exist anions such as chloride, nitrate, and sulfate was minimal in sorption capacity of the iron oxide for arsenic.