비정질 실리콘 박막 위에 구리용액을 스콘코팅하여 구리이온을 흡착시킨 후 이를 표면 핵생성 site로 이용하는 새로운 저온 결정화 방법에 관하여 연구하였다. 구리 흡착으로 LPCVD비정질 실리콘 박막의 결정화온도를 500˚C까지 낮출 수 있었고 결정화시간도 크게 단축되었다. 530-600˚C에서 어닐링시 구리가 흡착된 비정질 실리콘 막은 나뭇가지 형태의 fractal을 이루며 결정화되었다. 이때 fractal크기는 구리용액의 농도에 따라 30-300μm로 성장하였다. Fractal의 내부는 새 털 모양의 타원형 결정립으로 구성되어 있으며 TEM 에 의한 최종 결정립의 크기는 0.3-0.4μm로 intrinsic 비정질 실리콘 박막을 600˚C에서 어닐링하였을 때화 크기가 비슷하였다. 구리용액의 농도 증가에 따라 핵생성 활성화 에너지와 결정성장 활성화 에너지가 감소하였다. 결과적으로 구리 흡착이 표면에서 우선 핵생성 site를 증가시키고 핵생성 및 fractal 성장에 필요한 활성화 에너지를 모두 낮추어 저온에서도 결정화가 촉진되었음을 알 수 있었다.

We have synthesized the water-insoluble chitosan derivative, N-dithiocarboxy chitosan sodium salt, through the reaction of chitosan with carbon disulfide in the presence of alkali metal hydroxide, Chitosan itself has been prepared using chitin, one of the most abundant compounds in nature, as a starting material. To elucidate this natural polymer the capacity of adsorbing heavy metal ions, we have performed adsorption experiments using chitosan derivatives of various average molecular weights with different contents of sulfur. The effect of pH, adsorption time and temperature on adsorption efficiency was also studied. The adsorbent derived from chitosan of average molecular weight ranging 5,700~20,000 was shown to have the highest capacity of adsorbing heavy metal ions. Adsorbing efficiency was increased as the reaction time was increased and as the reaction temperature range of 25~45℃. The adsorption capacity at various pH, however, appeared to vary depending on the heavy metal ions studied.

아미드옥심기와 복합재료 섬유흡착제를 제조하였고 해수로부터 우라늄이온의 분리 특성을 조사하였다. 흡착량은 흡착시간이 증가함에 따라 증가하였고 An:TEGMA:DVB의 몰비가 1:0.1:0.003인 수지가 pH 8 부근에서 최대 흡착능을 나타내었다. 또한 흡착량은 CFA에 첨가한 흡착제의 양이 증가함에 따라 증가하였으며 1시간 까지 선형적으로 증가하였고, 25˚C에서 최대흡착량을 나타내었다. 한편 Ca, Mg 이온은 흡-탈착 cycle이 반복될수록 증가하였으며 그양은 각각 0.3, 0.9mmole/g-Ads로 우라늄 이온의 그것보다 매우 낮았다. 흡착된 우라늄 이온의 탈착은 흡착제의 종류에 관계없이 약 30분 이내에 거의 100% 탈착되었다.

Chitosan itself has been prepared using chitin, one of the most abundant compounds in nature, as a starting material. We have synthesized the water-soluble chitosan derivative, N-dithiocarboxy chitosan sodium salt, through the reaction of water-soluble chitosan with carbon disulfide in the presence of alkali metal hydroxide. To elucidate this natural polymer capacity of adsorbing heavy metal ions, we have performed adsorption experiments using the water-soluble chitosan derivative various average molecular weight and of different percent contents of sulfur. The effect of pH, adsorption time and temperature on adsorption efficiency was also studied. The adsorbent derived from water-soluble chitosan of average molecular weight ranging 9,000~120,000 was shown to have the highest capacity of adsorbing heavy metal ions. On the whole, adsorbing efficiency was increased as the reaction time goes longer and also increased as the reaction temperture goes higer in temperture range of 15℃~45℃. The adsorption capacity at various pH, however, was appeared to vary depending on the heavy metal ions studied Judging from these finding, water-soluble N-dithiocarboxy chitosan sodium salt, a derivative of a biodegradable nature polymer, is believed to be a potential adsorbent for heavy metal ions since it not only is shown to lower the concentration of heavy metal ions to below the drainage quality standard, but also it would not cause acidification and hardening of soil which is one of the detrimental effects of synthetic macromolecular adsorbents present.

본 연구는 흡착과 막분리를 결합시킨 혼성 시스템을 폐수처리에 응용하기 위한 기초 연구로서, 페놀을 분말활성탄에 의해 흡착하고, 흡착된 페놀을 활성탄과 함께 정밀여과에 의해 분리하였다. 분말활성탄의 입자크기가 클수록 여과저항은 감소하였으며, 활성탄의 양이 적을수록 단절점(break point) 이전의 투과농도 변화율과 페놀 부하 변화율은 증가하였다. 분말활성탄의 입자크기가 작을수록 활성탄의 외표면적과 경막물질전달계수의 증가로 인해 단절점 전의 투과농도는 감소하였다.

Diazotization of 2-Amino-5-nitrophenol was Synthesized by the direct diazotization method. The diazonium salts are usually stabilized in the from of double salts. The double salts of zinc chloride are the Commonest, and the double salt method is Specially applicable to the yield-up of coupling. The azo dye(2-naphthol-1-(2'-diazo-5'-nitrophenol)) is Converted into a chromium Complex by heating(100℃) with chromic formate, and DMF. The removal of inorganic salts from dyestuffs was performed in DMF solvent. This effect was more pronounced. From these results, It was obtained to liquid dyestuffs of metal complex with High fastness and high adsorption.

The occurrence of objectionable tastes and odors in drinking water is a common and widespread problem. The most troublesome odors are usually those described as muddy or earthy-musty. Two organic compounds which have been implicated as the cause of earthy-musty odor problems in water are geosmin and 2-Methylisoborneol. These earthy-musty organics have been shown to be metabolites of actinomycetes and blue green algae. The purpose of this paper is to describe adsorbability in removing these two oder causing compounds(geosmin and 2-MIB) upon various conditions like pH variation, adding humic acid and different activated carbon. The conclusion of this study are as followings. In batch test, carbon dosage is 10mg/100ml for geosmin and 15mg/100ml for 2-MIB. Both were in equilibrium state after 60 hours. In model simulation, F-P model described experiment data and modelling data appropriately in geosmin but F-S model not. In case of 2-MIB, models didn't describe relation between experiment and modelling data well. Two causative agents of earthy-musty odor compounds, geosmin and 2-MIB, are strongly adsorbed by activated carbon either coconut or brown. There appears to be no effect of pH (3,7,9) on adsorption of these two organics. Activated carbon proved to be more effective for removing geosmin than for removing 2-MIB. When activated carbon is. used in removing these two organics, the removal of these appeared to be adversely affected by back ground organic compounds, such as humic substances, due to competitive adsorption.

It is well known that the adsorption character of activated carbon is dependent on the specific surface area and pore volume, but the relationship between the surface-chemical structure and the adsorption character has not been studied very often. The purpose of this study is to investigate the effect of the acidic surface functional groups of activated carbon and the adsorption characteristics of low concentration phenol. So three types of activated carbons and four different treatments were introduced to this isotherm experiment. These treatments were nontreatment, 1N $HNO_3$ treatment, 6N $HNO_3$ treatment, $H_2O_2$ treatment. The conclusions of this study are as followings. If the initial concentration of phenol is high as 5mg/l, the adsorption is dependent on the specific surface area. If the initial concentration of phenol is low as $100{\mu}g/l$, the adsorption is dependent on the average pore volume. The acidic surface functional groups prevent the adsorption of phenol molecules to activated carbon. And the adsorbed amount decreases more for $HNO_3$ treatment than for $H_2O_2$ treatment and more for concentrated $HNO_3$ treatment than for dilute $HNO_3$ treatment.

Zeolite에 의(依)한 의 흡착반응(吸着反應)에 영향(影響)을 미치는 열처리(熱處理)에 의(依)해 조사(調査)하고 배양실험(培養實驗)을 통하여 Zeolite에 흡착(吸着)된 의 소실량(消失量)을 조사(調査)하였다. Zeolite의 주구성점토광물(主構成粘土鑛物) Clinoptiolite와 mordenite였다. Zeolite에 의(依)한 의 흡착반응(吸着反應)은 4시간(時間) 진탕으로 흡착평형(吸着平衡)에 도달(到達)하였다. 열처리온도(熱處理溫度)가 높을수록 치환성(置換性) 의 합량(合量)은 증가(增加)하였으나 의 흡착량(吸着量)은 감소(減少)하였다. 유안(硫安)을 처리(處理)한 토양(土壤)을 담수상태(湛水狀態)에서 배양(培養)한 결과(結果) 시간(時間)이 경과(經過)할수록 토양중(土壤中) 잔류량(殘留量)이 감소(減少)한 반면(盤面) Zeolite에 흡착(吸着)된 는 동일기간(同一期間) 내(內)에 소실(消失)되지 않았다. 그러므로 Zeolite에 흡착(吸着)된 은 여러 가지 작용(作用)에 의(依)한 소실(消失)에 대(對)해 저항성(抵抗性)이 크다고 할 수 있다.

Kaolinite, Zeolite 및 Montmorillonite에 Trifluralin을 첨가(添加)하여 흡착실험(吸着實驗)을 행하고 대맥(大麥)을 사용(使用)하여 점토(粘土) 현탁액중(懸濁液中)에서의 Trifluralin의 활성변화(活性變化)를 조사(調査)하였다 Trifluralin의 흡착량(吸着量)은 Montmorillonite>Zeolite>Kaolinite의 순서(順序)이었으며 점토량(粘土量)이 많아질수록 흡착량(吸着量)은 증가(增加)되었으나, 단위(單位) 중량당(重量當) 흡착량(吸着量)은 감소(減少)하였다. Trifluralin의 농도(濃度)가 높을수록 흡착량(吸着量)은 증가(增加)하였으며 각(各) 농도(濃度)에서 Montmorillonite가 가장 높은 Kd치(値)를 나타냈다. Trifluralin은 현탁액(懸濁液)의 pH변화(變化)에도 불구하고 흡착량(吸着量)의 차이(差異)는 없었다. 이는 점토(粘土) 표면(表面)에 Trifluralin이 물리적(物理的)인 힘에 의해서 흡착(吸着)된 것이라 판단(判斷)되었다. Trifluralin의 농도(濃度)가 증가(增加)함에 따라 대맥(大麥)의 생육(生育)은 조해(阻害)되었으나 점토광물(粘土鑛物)의 첨가(添加)로 대맥(大麥)의 생육조해율(生育阻害率)은 약간 감소(減少)되었다.

국내 포항 소재 R사의 구룡포산 천연 제올라이트의 물리·화학적 특성을 규명하기 위해 X-선 회절 분석, X-선 형광 분석, 열 시차·열 중량 분석, 양이온 교환능 분석 및 세슘(Cs), 스트론튬(Sr) 흡착 실험을 수행하였다. X- 선 회절 분석 결과 모데나이트, 휼란다이트, 클라이놉티로라이트 및 일라이트와 같은 광물이 함유되어 있으며, X- 선 형광 분석 결과 SiO2, Al2O3, CaO, K2O, MgO, Fe2O3 및 Na2O 원소가 함유되어 있었다. 양이온 교환능은 148.6 meq/100 g이었으며 열시차 및 열중량 분석 결과 600℃까지 열적으로 안정성이 우수한 것을 확인하였다. 시 간에 따른 흡착 평형 실험 결과 세슘(Cs)의 경우 30분이내 스트론튬(Sr)의 경우 8시간이내에 평형에 도달하였으며 세슘(Cs) 및 스트론튬(Sr)의 흡착률은 각각 80% 및 18%를 보이고 있었다. 단일 성분 등온 흡착 실험 결과 Langmuir model에 부합하였으며 세슘(Cs) 최대 흡착량은 131.5 mg/g으로 높게 나타났으며 반면 스트론튬(Sr) 최 대 흡착량은 29.5 mg/g로 낮은 흡착량을 나타내었다. 본 연구에 사용된 천연 제올라이트의 경우 클라이놉티로라 이트, 휼란다이트 및 모데나이트와 같은 8-ring을 포함하는 광물의 함량이 높아 세슘(Cs)에 대한 높은 선택성을 보 여주고 있다.

코발트는 합금산업에서 발생되는 산업 폐기물과 산성광산배수로 자연에 유입될 수 있으며 또한 고준위 방사성 폐기물을 구성하는 방사성 핵종(60Co)기도 하다. 스멕타이트는 이들을 흡착 격리하는데 유용하게 사용될 수 있는 광물이다. 본 연구에서는 기존에 특성이 잘 알려진 스멕타이트 중 The Clay Mineral Society (CMS)의 source clay인 Cheto-type montmorillonite (Cheto-MM)를 사용하여 가열에 의한 탈수 전후 광물의 층간수 존재 여 부에 따른 흡착 자리가 코발트 흡착에 미치는 영향을 평가하고, 흡착 속도 및 등온흡착식 모델을 적용하여 Cheto- MM의 코발트에 대한 흡착 기작을 연구하였다. 본 연구 결과 탈수 및 이에 따른 층간 수축에 의해 흡착 특성이 달 라지는 것을 확인할 수 있었으며, 코발트는 Cheto-MM의 층 모서리 자리에서의 흡착이 약 38%, 층간 내부에서의 흡착이 약 62%를 차지하는 것으로 확인되었고 Cheto-MM의 코발트 흡착은 층간 내부에 의한 영향이 큰 것으로 판 단된다. 이러한 흡착에 있어 흡착 속도 모델을 적용한 결과, Cheto-MM의 코발트 흡착 속도는 pseudo-second-order 모델로 설명되며 농도에 따른 흡착은 Langmuir 등온흡착 모델로 가장 잘 설명되었다. 본 연구는 몬모릴로나이트 의 흡착 자리에 따른 코발트의 흡착 양상에 대한 기본지식을 제공하고, 추후 고준위 방사성 폐기물 처분장에서의 스멕타이트의 흡착 거동을 예측하는데 유용하게 사용될 수 있을 것으로 생각된다.

A zeolite material (ZCH) was synthesized from coal fly ash in an HD thermal power plant using a fusion/hydrothermal method. ZCH with high crystallinity could be synthesized at the NaOH/CFA ratio of 0.9. Ion-exchanged ZCH adsorbents for ammonia removal were prepared by ion-exchanging various cation (Cu2+, Co2+, Fe3+, and Mn2+) on the ZCH. They were used to evaluate the ammonia adsorption breakthrough curves and adsorption capacities. The ammonia adsorption capacities of the ZCH and ion-exchanged ZCHs were high in the order of Mn-ZCH > Cu-ZCH ≅ Co-ZCH > Fe-ZCH > ZCH according to NH3-TPD measurements. Mn-ZCH ion-exchanged with Mn has more Brønsted acid sites than other adsorbents. The ion-exchanged Cu2+, Co2+, Fe3+, or Mn2+ ions uniformly distributed on the surface or in the pores of the ZCH, and the number of acidic sites increased on the alumina sites to form the crystal structure of zeolite material. Therefore, when the ion-exchanged ZCH was used, the adsorption capacity for ammonia gas increased.

The adsorption characteristics of four pesticides (phosphamidon, fenitrothion, triadimefon, and diniconazole) on natural clinoptilolite (CLIN) and three synthetic zeolites were investigated. The synthetic zeolites included faujasite (FAUF) synthesized from coal fly ash; the mixture of FAU and Na-P1 (FAU + Na-P1)SF synthesized using Jeju scoria and coal fly ash at the ratio of 1.5 by weight; and waste fluid catalytic cracking catalyst (FCCW). The distribution coefficient, KD and the Freundlich constant, KF decreased in the following sequence: FCCW > FAUF > (FAU + Na-P1)SF > CLIN among the zeolites and diniconazole>fenitrothion> triadimefon> phosphamidon among the pesticides. The pesticide adsorptivity increased with increasing temperature for FAUF, (FAU+Na-P1)SF and FCCW, however, it decreased for CLIN, regardless of the type of pesticide. The adsorptivity of pesticides was independent of pH for phosphamidon, fenitrothion and triadimefon, whereas it decreased with increasing pH for diniconazole, regardless of zeolite type.

A zeolite material with a Si/Al molar ratio of 1.2 was synthesized by changing the NaOH/CFA ratio of coal fly ash (CFA) via a fusion/hydrothermal reaction in the HD thermal power plant. The change in the crystal structure of the zeolite was confirmed using XRD and SEM, and the ammonia adsorption capacities of the synthesized zeolitic materials and a commercial zeolite (Na-A zeolite) were analyzed via an ammonia temperature-programmed desorption (NH3-TPD) process. The SEM and XRD results revealed out the zeolitic materials from the coal fly ash maintained a hexagonal Linde-type crystal structure similar to that of Na-A zeolite, but the crystallinity of the synthesized zeolitic material was reduced due to impurities. The NH3 adsorption capacity, determined from the NH3-TPD analysis of was 1.122 mmol/g of the synthesized zeolitic material, which was lower than the NH3 adsorption capacity of the Na-A zeolite.

Magnetic activated carbon was prepared by adding a magnetic material to activated carbon that had been prepared from waste citrus peel in Jeju. The adsorption characteristics of an aqueous solution of the antibiotic trimethoprim (TMP) were investigated using the magnetic activated carbon, as an adsorbent, and response surface methodology (RSM). Batch experiments were carried out according to a four-factor Box-Behnken experimental design affecting TMP adsorption with their input parameters (TMP concentration: 50～150 mg/L; pH: 4～10; temperature: 293～323 K; adsorbent dose: 0.05～0.15 g). The significance of the independent variables and their interaction was assessed by ANOVA and t-test statistical techniques. Statistical results showed that TMP concentration was the most effective parameter, compared with others. The adsorption process can be well described by the pseudo-second-order kinetic model. The experimental isotherm data followed the Langmuir isotherm model. The maximum adsorption capacities of TMP, estimated with the Langmuir isotherm model were 115.9-130.5 mg/g at 293-323 K. Also, both the thermodynamic parameters, △H and △G, have both positive values, indicating that the adsorption of TMP by the magnetic activated carbon is an endothermic reaction and proceeds via an involuntary process.

Zeolitic material, Z-Y3, was synthesized from coal fly ash (CFA) under low-alkaline conditions (NaOH/CFA ratio = 0.3 and NaOH solution concentrations of 0.0, 0.5, and 1.0 M) using a fusion/hydrothermal method. The adsorption capacities of the fabricated Z-Y3 samples for Cs and Sr ions and the desorption capacity of Na ions were evaluated. The XRD patterns of the Z-Y3 sample fabricated using a 1.0 M NaOH solution (Z-Y3 (1.0 M)) indicated the successful synthesis of a zeolitic material, because the diffraction peaks of Z-Y3 coincided with those of the Na-A zeolite in the 2θ range of 7.18-34.18. Moreover, the SEM images revealed that morphology of the Z-Y3 (1.0 M) sample, which presented zeolitic materials characteristics, consisted of sharp-edged cubes. The adsorption isotherms of Cs and Sr ions on all the fabricated Z-Y3 samples were described using the Langmuir model, and the maximum adsorption capacities of Cs and Sr were calculated to be 0.14-0.94 mmol/g and 0.19-0.78 mmol/g, respectively. The desorption of Na ions from the Cs and Sr ions adsorbed Z-Y3 samples followed the Langmuir desorption model. The maximum desorption capacities of Na ions from the Cs and Sr ions adsorbed Z-Y3 (1.0 M) samples were 1.28 and 1.49 mmol/g, respectively.

토양과 지하수에서 미세플라스틱과 나노플라스틱이 검출되면서 자연환경에서의 플라스틱 입자에 대 한 거동 연구 필요성이 강조되고 있다. 자연환경에서 풍화과정을 통해 생성되는 2차 나노플라스틱은 그 양이 많을 것으로 예상되지만, 토양과 지하수 내 나노플라스틱에 대한 연구는 분석 기술의 제약으로 인해 플라스틱 거 동 연구가 부족한 상태이다. 이번 연구에서는 수 ng/cm2 수준의 흡착량을 측정할 수 있는 수정진동자미세저울 (quartz crystal microbalance, QCM)의 광물표면-나노플라스틱 상호작용 규명연구 활용 가능성을 확인하였다. 일반 컬럼실험에서는 SiO2 표면과 폴리스티렌(polystyrene) 나노플라스틱의 흡착을 관찰하기 위해 담수나 지 하수의 이온세기 수준을 넘거나 높은 농도의 나노플라스틱을 주입하는데, 이번 QCM 실험에서는 컬럼실험에 서 측정이 불가능한 낮은 이온세기와 플라스틱 농도에서 나노플라스틱의 흡착량을 측정할 수 있었다. 광물표 면과 나노플라스틱의 상호작용 나아가 토양과 지하수 자연환경에서 나노플라스틱 거동을 이해하는 데 QCM 연구가 크게 기여할 것으로 기대된다.

In this study, zeolitic materials were synthesized from Jeju Volcanic Rocks (JVR) using a fusion/hydrothermal method at NaOH/JVR ratios of 0.6 and 1.2. The crystallinities of the zeolitic materials at NaOH/JVR ratios of 0.6 and 1.2 were 25.5% and 59.0%, respectively. It was confirmed through the SEM image that the zeolitic materials covered the zeolite particle with a cube-shaped crystals. The Co ions adsorption by the zeolitic materials were to reach the adsorption equilibrium at 120 min. It could be better simulated in the pseudo-second order adsorption kinetic equation than in the pseudo-first order adsorption kinetic equation. The adsorption capacities (qm) of Co ions could be to estimate Langmuir isotherm better than Freundlich isotherm. The maximum adsorption capacities (qm) at NaOH/JVR ratios of 0.6 and 1.2 were 55.3 mg/g and 68.7 mg/g, respectively. It was found that there was a high correlation between the crystallinity of zeolitic materials and the adsorption capacity of Co ions adsorption.