• 대한화학회지
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• 제17권4호
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• pp.269-274
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• 1973

${\alpha}$-Cyano-${\beta}$-Piperonylacrylic Acid의 가분해 속도상수를 자외선분광기를 사용하여 구하였으며 아울러 넓은 pH범위에 잘 맞는 반응속도식도 얻었다. 이 식에 의하면 넓은 pH범위에 잘 맞는 반응속도식도 얻었다. 이 식에 의하면 넓은 pH범위, 특히 종전에 잘 규명된 바 없는 산성용매 속에서의 반응 및 hydroxide ion의 촉매역활 등도 정략적으로 잘 설명할 수 있음을 알았다. 즉 pH4.0이하에서의 가수분해반응은 ${\alpha}$-Cyano-${\beta}$-Piperonylacrylic Acid에 물분자가 첨가되므로써 시작되며 pH $5.0{\sim}7.5$ 에서는 ${\alpha}$-Cyano-${\beta}$-Piperonylacrylic Acid와 ${\alpha}$-Cyano-${\beta}$${\alpha}$-Cyano-${\beta}$-piperonylacrylate anion에 물분자만이 첨가되며 pH 12.0 이상에서는 hydroxide ion만이 ${\alpha}$-Cyano-${\beta}$-piperonylacrylate anion에 첨가됨을 알았다.

• 멤브레인
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• 제19권3호
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• pp.189-193
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• 2009

제올라이트 분리막 제조 시 제올라이트 골격 내에 존재하는 $Na^{+}$ 양이온을 $K^{+}$ 이온과 $Ca^{2+}$ 이온으로 교환하여 보다 효율적인 물/에탄올 혼합물로부터 물의 분리를 도모하고자 하였다. NaA형 제올라이트 분리막을 각각의 0.5 M KCI $CaCl_2$, $80^{\circ}C$ 수용액에서 4시간 동안 이온교환 하였다. $Na^{+}$ 이온을 $K^{+}$ 이온으로 교환한 결과, 이온 교환 전 총 투과플럭스는 $900\;g/m^2{\cdot}hr{\sim}2,500\;g/m^2{\cdot}hr$이었으나 이온 교환 후 $600\;g/m^2{\cdot}hr{\sim}2,000\;g/m^2{\cdot}hr$ 정도로 낮아졌으며, 이온 교환 전 $600{\sim}2,200$의 선택도를 나타내던 분리막의 선택도가 이온 교환 후에 $850{\sim}2,500$까지 높아짐을 확인하였다 또한, $Na^{+}$ 이온을 $Ca^{2+}$ 이온으로 교환한 결과, 제올라이트 분리막의 전체 투과플럭스와 선택도 모두 이온 교환 전 후 유사한 결과 값이 나타남을 확인하였다. 따라서 친수성 제올라이트 분리막의 유효세공경을 제어하고 적절한 크기로 조절하여 유기물/물 혼합물 분리에 활용한다면 보다 효과적인 유기물의 선택적 분리가 가능할 것으로 판단된다.

• 환경위생공학
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• 제21권4호
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• pp.29-38
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• 2006

This study included the development of analytical method for determining perchlorate in water sample. The analytical condition was referred in EPA 314.0 method which use ion chromatography and the concentrator column was replaced by the guard column. Concentrating 10mL raw or treated water sample on to AGl6 guard column made it possible to get the LOD(Limit of Detection) of $0.73\;{\mu}g/L$. The total run time was 11 minutes and during run time next sample could be concentrated on AGl6 guard column. Compared to the Concentration method which needed manual operation, the Direct Injection method could screen the many water samples. The LOD of the Direct Injection method was higher and the sensitivity was lower than that of the Concentration method. The RSDs(Relative Standard Deviations) were lower than 2.5 % for peak height and 0.7 % for retention time in pre-concentration methods. This method Showed good reproducibility and reliability and it was thought the deviations of recovery value could be reduced by considering column capacity and making water sample homogeneous. Matrix Elimination could be done using the pre-concentration method if perchlorate were in complex matrix of sample.

• 폴리머
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• 제26권5호
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• pp.575-581
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• 2002

본 연구는 폴리에틸렌 기재에 비드와 섬유상 이온교환체의 배합비를 달리하여 불균질 이온 교환막을 제조하였다. PE 불균질 이온교환막의 이온교환능은 섬유강 이온교환체의 양이 증가할수록 선형적으로 증가하였으며 30 wt%에서 최대 1.86 meq/g 이었다. 불균질 이온교환막의 함수율, 고정이온농도 및 이온운반율도 섬유상 이온교환체의 양이 증가할수록 증가하였나. 반면 불균질 이온교환막의 전기저항은 섬유상 이온교환체의 양이 증가할수록 감소하였으며, IXF (ion exchange fiber)의 혼합량이 30 wt%에서 5$\Omega$/$\textrm{cm}^2$으로 전기저항 값이 가장낮았다.

• 공업화학
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• 제28권4호
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• pp.410-419
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• 2017

지구온난화, 환경오염, 가뭄 등의 재해현상으로 인한 물 부족 현상이 진행됨에 따라 수자원의 활용성을 증가시키기 위한 원천기술의 개발과 연구들이 진행되고 있다. 그중 수처리 분리막 기술은 기존 물리화학적 및 생물학적 공정보다 수질 개선 효과가 우수하고 약품 사용이 배제된 환경친화적인 공정이다. 수처리 분리막은 오폐수처리, 정수처리, 해수담수처리, 이온교환 공정, 초순수 제조, 유기용매 분리 등 다양한 분야에 적용되며 분리막을 이용한 수처리 기술은 점차 응용 범위가 넓어지고 있는 추세이다. 수처리 분리막의 핵심 기술은 분리성능을 조절하기 위한 기공 사이즈를 조절하는 것으로써 더 나은 성능을 나타내는 분리막을 개발하기 위한 연구가 활발히 진행되고 있다. 본 총설에서는 수처리용 분리막의 특허 및 논문의 기술경쟁력 평가를 통하여 국가별, 기관별 발표 빈도수를 정리하였으며, 오폐수처리용 분리막, 정수처리용 분리막, 해수담수화용 분리막, 그리고 이온교환공정용 분리막에 대한 평가를 진행하고, 향후 연구 방향에 대하여 제시해 보고자 한다.

• 상하수도학회지
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• 제21권4호
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• pp.375-383
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• 2007

Treatment efficiency research was performed using Fenton process and the electrochemical process in the presence of ferrous ion and hydrogen peroxide for the industrial wastewater including 1,4-Dioxane produced during polymerization of polyester. The Fenton process and the electrochemical Iron Redox Reaction (IRR) process were applied for this research to use hydroxyl radical as the powerful oxidant which is continuously produced during the redox reaction with iron ion and hydrogen peroxide. The results of $COD_{Cr}$ and the concentration of 1,4-Dioxane were compared with time interval during the both processes. The rapid removal efficiency was obtained for Fenton process whereas the slow removal efficiency was occurred for the electrochemical IRR process. The removal efficiency of $COD_{Cr}$ for 310 minutes was 84% in the electrochemical IRR process with 1,000 mg/L of iron ion concentration, whereas it was 91% with 2,000 mg/L of iron ion concentration. The lap time to remove all of 1,4-Dioxane, 330 mg/L in the wastewater took 150 minutes with 1,000 mg/L of iron ion concentration, however it took 120 minutes with 2,000 mg/L of iron ion concentration in the electrochemical IRR process.

• 멤브레인
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• 제27권2호
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• pp.109-120
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• 2017

양이온($Na^+$) 및 음이온($Cl^-$)이 각각의 CEM과 AEM을 통해 선택적으로 분리되어 담수로 이동할 때 발생되는 전위차와 산화/환원(redox couple)형 전해질을 포함하고 있는 전극에서 발생하는 전류를 이용하여 전기 에너지로 전환시키는 에너지변환장치이다. RED 시스템의 핵심소재 중 하나인 이온교환막은 높은 출력 밀도를 달성하기 위해 1) 낮은 팽윤거동, 2) 적절한 이온교환능, 3) 높은 이온전도도, 4) 높은 이온선택성을 만족시켜야 한다. 본 논문에서는 이를 만족시키는 소재 및 이온교환막의 연구동향 및 전망에 대해 설명하였다.

• Journal of Applied Biological Chemistry
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• 제43권1호
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• pp.18-24
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• 2000

A one-dimensional transport of displacing monovalent ion, $A^+$, and a trivalent ion being displaced, $B^{3+}^ in a porous exchange system such as soil was approximated using the Crank-Nicolson implicit finite difference technique and the Thomas algorithm in tandem. The variations in the concentration profile were investigated by varying the ion-exchange equilibrium constant (k) of ion-exchange reactions, the influent concentrations, and the cation exchange capacity (CEC) of the exchanger, under constant flux condition of pore water and dispersion coefficient. A higher value of k resulted in a greater removal of the native ion, behind the sharper advancing front of displacing ion, while the magnitude of the penetration distance of $A^+$ was not great. As the CEC increased, the equivalent fraction of $B^{3+}^ initially in the soil was greater, thus indicating that a higher CEC adsorbed trivalent cations preferentially over monovalent ions. Mass balance error from simulation results was less than 1%, indicating this model accounted for instantaneous charge balance fairly well.

• 한국진공학회:학술대회논문집
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• 한국진공학회 1999년도 제17회 학술발표회 논문개요집
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• pp.202-202
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• 1999

The Polyethylene (PE), Polystyrene (PS) and Polytetrafluoroethylene (PTFE) surface modification was investigated by hydrogen io assisted reaction (H-IAR) in oxygen environment. The IAR is a kind of surface modification techniques using ion beam irradiation in reactive gas environment. The energy of hydrogen ion beam was fixed at 1keV, io dose was varied from 5$\times$1014 to 1$\times$1017 ions/$\textrm{cm}^2$, and amount of oxygen blowing gas was fixed 4ml/min. Wettability was measured by water contact angles measurement, and the surface functionality was analyzed by x-ray photoelectron spectroscopy. The contact angle of water on PE modified by argon ion beam only decrease from 95$^{\circ}$ to 52$^{\circ}$, and surface energy was not changed significantly. But, the contact angle using hydrogen ion beam with flowing 4ml/min oxygen stiffly decreased to 8$^{\circ}$ and surface energy to 65 ergs/cm. In case of PS, the contact angle and surface energy changes were similar results of PE, but the contact angle of PTEE samples decreased with ion dose up to 1$\times$1015 ions/$\textrm{cm}^2$, increased at higher dose, and finally increased to the extent that no wetting was appeared at 1$\times$1017 ions/$\textrm{cm}^2$. These results must be due to the hydrogen ion beam that cleans the surface removing the impurities on polymer surfaces, then hydrogen ion beam was activated with C-H bonding to make some functional groups in order to react with the oxygen gases. Finally, unstable polymer surface can be changed from hydrophobic to hydrophilic formation such as C-O and C=O that were confirmed by the XPS analysis, conclusionally, the ion assisted reaction is very effective tools to attach reactive ion species to form functional groups on C-C bond chains of PE, PS and PTFE.

• 한국물환경학회지
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• 제22권1호
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• pp.116-121
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• 2006

Fundamental investigations have been carried out to find the applicability of manganese nodule as an adsorbent of nickel ion with an intention that nickel can be secured in manganese nodule along with the treatment of wastewater. The average content of manganese in nodules which used in the experiments was about 27%. The content of nickel in manganese nodules was observed to increase up to 4 times higher with comparison to its original value after adsorption. When the initial concentration of nickel ion in artificial wastewater was lower than 500 mg/L, its adsorbed amount on manganese nodule was shown to increase continuously. However, no more than about 82 mg/L of nickel was attained at higher initial nickel ion concentration than 500 mg/L. The adsorption of nickel ion was increased with temperature under experimental conditions and as the size of manganese nodule particles became smaller more nickel ion was adsorbed on adsorbent. Regarding the effect of pH, the adsorption of nickel ion was more hindered as the solution became acidic. Adsorption behavior of nickel ion on manganese nodule was found to follow the Freundlich model well and kinetic analysis showed that the adsorption reaction of nickel ion was second order. Thermodynamic parameters for the nickel ion adsorption were estimated on the basis of thermodynamic equations and they were in good agreement with experimental results.