• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 1997.05a
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• pp.97-100
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• 1997

본 연구에서는 알루미늄 제작 공정에서 폐기물로 발생하는 gibbsite를 이용하여 용액 내에 존재하는 인산염을 제거하였다. 실험을 수행함에 있어 용액의 pH를 3, 7, 10으로 변화시켜 보았고 인산염 제거에 미치는 여러 인자들 중에서 P : Al 의 비율이 미치는 영향을 살펴보고자 인산염의 농도를 100, 200, 500, 800, 1000 mg/l 로 변화시켰으며, gibbsite 의 양을 2, 4, 8, 10 g 으로 변화시켜 실험하였다. 이러한 실험 결과로부터 72 hr 이후에 용액 내의 인산염 농도가 일정하게 유지된다는 것을 알 수 있있다. 인산염의 제거율은 pH가 낮을수록 높아졌다. 또한 인산염의 초기농도가 낮을수록 제거율이 높아졌으며, 투여된 gibbsite 의 양이 많을수록 제거율이 높아지는 것으로 나타났다.

• Resources Recycling
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• v.12 no.4
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• pp.38-43
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• 2003

Phosphate is an essential material for the growth of organisms. However. since relatively small amount is required. a large amount of phosphate is abandoned in wastes and wastewater. which contaminate the ecological environment including aquatic system. Purpose of this study is to treat especially high concentrated phosphate wastewater by use of calcium precipitation method. The pH range considered was from 6 to 12 and the maximum removal of phosphate was attained at pH 12. The con-centration of phosphate was observed to decrease rapidly until a half amount of calcium ion to its equivalent for the formation of calcium phosphate precipitate was added. which resulted in the decrease of the remaining concentration of phosphate down to 0.0027 mM. The effect of fluoride ion was examined and the concentration ratio between the phosphate and fluoride ion did not have any significant influence on the removal efficiency of phosphate. The effect of pH was also investigated. With the increasing of the pH in solution, the removal rate of phosphate was increased. Also it was investigated that the effect of fluoride on the phosphate removal was not significant.

• Proceedings of the Korean Radioactive Waste Society Conference
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• 2009.06a
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• pp.296-296
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• 2009

산화물 사용후핵연료를 대상으로 하는 파이로 공정은 고온 용융염 매질에서 산화물을 금속으로 전환시키는 전해환원 공정으로부터 시작된다. 이후, 전해정련 공정이 도입되어 전해환원 공정에서 금속으로 환원된 생성물을 처리하게 된다. 전기화학적 공정인 이 두 공정에는 전류전달 매질인 전해질로 용융염이 사용된다. 그러나 전해환원 공정은 LiCl 염을 기반으로 하는 반면 전해정련은 LiCl-KCl 공융염 조건에서 운전하여 두 공정의 연계성 향상 및 공정 안정성 확보를 위해서는 전해환원 공정에서 생성되는 금속전환체에 존재하는 잔류염을 제거하는 공정의 도입이 두 공정사이에 고려되고 있다. 전해환원 공정에서 산화물이 금속으로 환원되는 동안 고체입자의 외형이 유지되며 따라서 제거된 산소에 의해 금속전환체에는 공극이 발생하게 된다. 또한, 전해환원에 도입되는 산화물의 물리적 형태가 분말 또는 펠렛 등 다양한 형태로 도입 가능하여 단위 입자들 사이에 많은 공극이 발생하게 된다. 이렇게 기존재하거나 또는 공정 운전에 의해 새롭게 생성된 공극에는 전해환원 매질인 LiCl 염이 침투하여 금속전환체는 염에 의해 젖게 되며 공정 종료시 고화되어 금속전환체에 포함된다. LiCl을 제거하기 위해서는 가열에 의한 증류가 연구되고 있다. 그러나 LiCl의 낮은 증기압에 의해 비교적 낮은 온도에서 증발시키기 위해서는 감압조건이 필수적으로 고려되어야 한다. 한국원자력연구원에서는 다공성 모의 금속전환체를 사용하여 LiCl에 의한 Wetting 후 적절한 증발 조건 결정을 목적으로 온도 및 압력 조건 설정을 위한 기초실험에 결과를 수행하였다. 본 연구의 기초 실험 결과 $700^{\circ}C$온도 조건과 감압조건이 잔류염 제거를 위한 공정조건임을 밝혔다. 또한 모의 금속전환체를 담고 있는 미세 다공성 Basket은 고온조건에서 공극의 변형에 의해 증발에 대한 저항으로 작용하여 증발 효율을 저하시키는 것으로 나타났다. 따라서 잔류염 제거를 위해서는 전해환원 Basket이 비교적 큰 공극을 지녀야 할 것으로 판단된다.

• Journal of the Korean Society of Marine Environment & Safety
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• v.22 no.7
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• pp.829-835
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• 2016

An excess in the nutrients such as nitrogen and phosphate leads to a phenomenon called eutrophication. In order to avoid this, numerous methods have been used to remove excess nutrients in the water. In this study, the use of a chemical method was assessed through the formation of magnesium ammonium phosphate. The difference in the removal efficiency of seawater and sea salt solution as primary sources of $Mg^{2+}$ ions and $Ca^{2+}$ ions for the formation of magnesium ammonium phosphate (MAP) and hydroxyapatite (HAP) respectively, were observed, taking into account the changes in pH and concentration. The results showed that seawater removed about 90 % phosphate and less than 50 % ammonia in sewage water condition, whereas the sea salt solution removed almost 90 % phosphate and 70 % ammonia in solution at pH 9 and 10 mM concentration of sea salt which further increases as the optimum ${Mg/PO_4}^{3-}$, ${NH_4}^+$ ratio reaches 2. The difference in the removal efficiency of seawater and sea salt was due to the fact that the set-ups were prepared in different conditions. This study suggests that both seawater and sea salt can be used to remove nutrients from the water. The relatively higher removal of phosphate can be explained by the formation of HAP from free $Ca^{2+}$ ions initially present in seawater and sea salt solution.

• Journal of Korean Society of Environmental Engineers
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• v.30 no.6
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• pp.637-641
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• 2008

The aims of this research were to manufacture tailored powder activated carbon having a higher prechlorate removal efficiency and to compare perchlorate removal efficiency with different carbon materials for applying to the drinking water treatment plant. Activated carbon pre-loaded with cetyltrimethylammonium chloride(CTAC) has been researched to be an effective adsorbent for removing perchlorate in the water. 10,000 mg/L tailored powder activated carbon were manufactured by mixing 5.0 g of powder activated carbon(PAC) into 500 mL of 5,000 mg/L CTAC solution. The tailored powder activated carbon had 10 times higher perchlorate removal efficiency than virgin powder activated carbon. The residual perchlorate gradually decreased with the first 15 minute contact time with the tailored powder activated carbon, however, the longer contact time did not affect perchlorate removal. Tailored powder activated carbon by manufactured with 1,083 mg/g iodine value carbon had almost 4 times higher perchlarate removal efficiency than the 944 mg/g iodine value carbon. Dosage of 5 mg/L tailored powder activated carbon, which can adaptable dosage at the treatment plant, could decrease the perchlorate concentration from 50 $\mu$g/L to 15 $\mu$g/L.

• Journal of the Korea Academia-Industrial cooperation Society
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• v.8 no.2
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• pp.372-379
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• 2007

The converter slag can be used to remove phosphate ion into the form of solid state from the wastewater. This research aims to evaluate the change of pH, alkalinity, leaching of positive ion in the wastewater and the removal of phosphate from the initial condition of wastewater. The change of pH was abruptly increased upto pH 11 for the initial condition of pH from 7.0 to 8.5 fer 0.5 unit of pH. The alkalinity was steadily increased from 10 hours of reaction time not same as pH increase. The removal of phosphate was very effective till 10 hours of reaction then it was slow after that time. The positive ion, magnesium ion was leached from the concentration of 2.0 mg/L to 4.3mg/L at the reaction time of 27 hours and 36 hours. Therefore, converter slag can be used to remove the phosphate in the form of Struvite from the wastewater.

• Proceedings of the KOR-BRONCHOESO Conference
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• 1991.06a
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• pp.35-35
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• 1991

식도이물은 대부분 상부식도에 위치하며 식도경술로 제거가 용이하지만 식도 점막내 매복된 이물이나, 식도경술의 합병증으로 인한 천공에 의하여 위급한 종격동염을 유발하는 경우가 있다. 이러한 종격동염은 하부식도에 위치한 이물 특히, 날카롭거나 표면이 불규칙하며 큰 경우에 유발하기 쉬우므로 초기에 개흉술을 통한 제거 또는 배농술 등의 적극적인 치료가 필요하다. 저자들은 1980년부터 1990년까지 10년간 본원에서 식도이물 제거술후 종격동염이 발생되어 개흉술 또는 배농술을 시행 받은 4례(틀니 1례, 칫솔 1례, 조개 껍질 1례, 생선 가시 1례)를 문헌고찰과 함께 보고하는 바이다.

• Journal of Navigation and Port Research
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• v.36 no.6
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• pp.459-463
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• 2012

In the present study, experiments have been performed to investigate the effects of the type of adsorbent, pH, and ionic strength on the adsorption of nutrients (nitrate and phosphate in artificial solution) onto the dredged sediment from a coastal fishery. In addition, this study aims to evaluate the possibility of removing the nutrients from the water using the dredged sediment. In the adsorption experiments of the nutrients, the reactions were completed within 10 minutes using ${NO_3}^-$-N($100{\mu}M$, 10mM) and ${PO_4}^{3-}$-P($100{\mu}M$, 10mM). In the steady state, 61% and 77% of the initial amounts were removed respectively for $100{\mu}M$ ${NO_3}^-$-N and $100{\mu}M$ ${PO_4}^{3-}$-P. The thermal treatment of the dredged sediment at $900^{\circ}C$ was not helpful to increase the removal efficiencies of the nutrients. Additives such as CaO and MgO dropped the removal efficiency of ${NO_3}^-$ to 0%, but increased that of ${PO_4}^{3-}$ up to 98%. Adsorption isotherms of ${NO_3}^-$ and ${PO_4}^{3-}$ could be explained by the Freundlich equation ($R^2$>0.99). The adsorption reaction was little influenced by the pH and ionic strength. Based on the results showing short reaction time and considerably high removal efficiencies of the nutrients, it is proposed to apply the dredged sediment from a coastal fishery to removing nutrients such as nitrate and phosphate in the water.

• Proceedings of the KSEEG Conference
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• 2001.04a
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• pp.4-6
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• 2001

• Applied Chemistry for Engineering
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• v.3 no.2
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• pp.349-359
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• 1992

Studies were carried out on the selective removal of inorganic salts such as NaCl and $Na_2SO_4$ from dye solution, using counter diffusion-reverse osmosis and nanofiltration, respectivey. For the dye solution used in the experiments, 1 to 30% of salts were removed by counter diffusion while the loss of dye molecules was less than 0.3%. The separation factors by one pass operation were 10-500 according to ionic species. In five successive operations, removals of anion($Cl^-$) increased but those of cation($Na^+$) decreased due to the Donnan effect. Effects of feed flow rate on removal efficiencies of various ions were also observed at constant flow rate of stripping water. Reverse osmosis of desalted dye solution by counter diffusion was conducted to prepare highly concentrated liquid dyes. The rejection efficiency of dye molecules was greater than 99%. For the rejection efficiency of chloride ion, experimental values were compared with theoretical ones based on solution-diffusion model. Two stage diafiltration was performed in nanofiltration. The rejection efficiency of chloride ion was continuously decreased due to the Donnan dialysis and even negative rejection was observed. The Donnan effect was more pronounced in the second diafiltration.