• 한국안전학회지
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• 제6권3호
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• pp.5-11
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• 1991

To remove NO from flue gas, a direct decomposition method to $N_2$ and $O_2$ was investigated by using copper / zeolite catalyst. The copper ion-exchanged HY type zeolite has high activity on NO decomposition. The decomposition activity was increased with the increase of ion-exchange level, contacting time and reaction temperature in the range of 30$0^{\circ}C$ -50$0^{\circ}C$ , and decreased with the oxygen addition.

• 한국재료학회지
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• 제11권2호
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• pp.120-125
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• 2001

흡착재료에는 hydroxyapatite(HAp), zeolite,, 분자체탄소, 활성탄, 알루미나등의 재료가 많이 사용되고 있다. 이들 흡착재료 중에서 금속이온과 양이온 교환반응이 좋은 HAp, zeolite는 폐수처리과정에서 많이 사용되고 있지만, 피러나 이 폐수처리과정에서 문제되는 것은 유해한 중금속뿐만 아니라 많은 세균들이 이 폐수에 존재하고 있어 수질오염 등의 여러 가지 문제를 야기 시키고 있다. 본 연구는 여러 중금속 흡착재료 중에서 HAp, zeolite에 항균효과가 있다고 알려진 금속이온 (Ag$^{+}$, Cu$^{2+}$, $Zn^{2+}$)들을 이온 치환시켜 항균성을 흡착재료에 부여하고자 한다. HAp, zeolite에 Ag$^{+}$, Cu$^{2+}$, $Zn^{2+}$의 금속이온들을 치환시킨 후, E. Coli로 항균효과를 측정하였다. HAp, zeolite와 여러 금속이온 치환후의 항균효과를 측정한 결과, Ag$^{+}$ 로 이온치환 시킨 HAp, zeolite에서는 1$\times$$10^{-2}$cell/ml 농도의 E. Coli에서 24시간가지 완벽한 항균효과를 보였고, Cu$^{2+}$와 $Zn^{2+}$으로 이온치환 시킨 경우에서는 좋은 항균효과를 보이지 않았다. 이러한 결과는 Feng. et. al.이 발표한 바와 같이1) Ag ion이 cell내부의 DNA에 영향을 기척, 복제능력을 떨어뜨리고 Cell을 비활성화 시키기 때문이다.

• 한국수처리학회지
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• 제26권6호
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• pp.13-26
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• 2018

This research was conducted to elucidate the removal mechanism of heavy metals and sulfate ion from acid mine drainage(AMD) by porous zeolite-slag ceramics (ZS ceramics) packed in a column reactor system. The average removal efficiencies of heavy metals and sulfate ion from AMD by the 1:3(Z:S) porous ZS ceramics in the column reactor under the HRT condition of 24 hours were Al 97.5%, As 98.8%, Cd 86.1%, Cu 96.2%, Fe 99.7%, Mn 64.1%, Pb 97.2%, Zn 66.7%, and $SO_4{^{2-}}$ 76.0% during 121 days of operation time. The XRD analysis showed that the ferric iron from AMD could be removed by adsorption and/or ion-exchange on the porous ZS ceramics. In addition it was known that Al, As, Cu, Mn, and Zn could adsorb or coprecipitate on the surface of Fe precipitates such as schwertmannite, ferrihydrite, or goethite. The EDS analysis revealed that Al, Fe, and Mn, which were of relatively high concentration in the AMD, would be adsorbed and/or ion-exchanged on the porous ZS ceramics and also exhibited that Al, Cu, Fe, Mn, and Zn could be precipitated as the form of metal hydroxide or sulfate and adsorbed or coprecipitated on the surface of Fe precipitates. The microscopic results on the porous ZS ceramics and precipitated sludge in a column reactor system suggested that the heavy metals and sulfate ion from AMD would be eliminated by the multiple mechanisms of coprecipitation, adsorption, ion-exchange as well as precipitation.

• 한국환경과학회지
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• 제20권11호
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• pp.1437-1445
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• 2011

The adsorption performance of lead ion was studied using five zeolites (Na-P1, sodalite (SOD), analcime (ANA), nepheline hydrate (JBW), cancrinite (CAN)) synthesized from Jeju scoria. The adsorption performances of lead ion decreased in the order of Na-P1 > SOD > ANA > JBW > CAN. These results showed that the synthetic zeolite with a higher cationic exchange capacity showed a higher adsorption performance. The uptake of lead ion by synthetic zeolites were described by Freundlich model better than Langmuir model. The adsorption kinetics of lead ion by synthetic zeolites fitted the pseudo 2nd order kinetics better than pseudo 1st order kinetics. The effective diffusion coefficients of lead ion by synthetic zeolites were ten times higher than the zeolite A synthesized from coal fly ash.

• 멤브레인
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• 제18권3호
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• pp.250-255
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• 2008

열적, 기계적, 화학적 안정성이 우수한 제올라이트 분리막의 물/에탄올 선택도를 이온교환 실험을 통해 더욱 효과적으로 높이고자 하였다. KA형 제올라이트 분리막을 직접 합성하는 것은 용이하지 않으므로 NaA형 제올라이트 분리막을 합성한 후 이를 다시 이온교환 하여 KA형 제올라이트 분리막을 제조하였다. 공급되는 에탄올의 농도 변화 및 투과 증발실험 온도의 변화가 투과플럭스와 물 선택도에 미치는 영향을 고찰하였다. 이온교환 실험 후 전체 투과플럭스는 감소하였고 물 선택도는 증가함을 관찰할 수 있었다.

• 한국환경과학회지
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• 제11권1호
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• pp.75-83
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• 2002

The removal performance of copper ion was studied using Na-P1 zeolites synthesized from Jeju scoria. The scoria which is found in large amounts in Jeju Island, was sampled at four regions, Jeju-shi Bonggae-dong(A). Pukcheju-gun Hanlim-eup Sangmyong-ri Mangoreum(B), Pukcheju-gun Hanlim-eup Keumag-ri(C) and Namcheju-gun Andeok-myun Dongkwang-ri(D). Synthetic Na-P1 zeolites used in this study were more effective than natural zeolite and scoria for the removal of copper ion. The removal performances of copper ion decreased in the order of Na-P1(D) > Na-P1(C) > Na-P1(B) > Na-P1(A) among Na-P1 synthesized from the scoria according to region. These results showed the same trend with cation exchange capacity(CEC) for each synthetic zeolite, i.e., the synthetic Na-P1 zeolite with a higher CEC showed a higher removal performance. The effective diffusion coefficients of copper ion by synthetic Na-P1 zeolites were one hundred and ten times higher than those by a pure zeolite 4A and the zeolite A synthesized from coal fly ash, respectively.

• 한국수자원학회:학술대회논문집
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• 한국수자원학회 2005년도 학술발표회 논문집
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• pp.1312-1316
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• 2005

Due to the Typhoon MAEMI on Sep. of 12 in 2003, the turbidity value of IMHA Dam was recorded more than 213NTU until now. The natural zeolite located in the east coast of Korean peninsula was applied to reduce turbidity with ion exchange Process. The result of this technique, the value of turbidity was reduced less than 1NTU. Also the value of pH showed stable state compare to before and after.

• 한국물환경학회지
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• 제23권5호
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• pp.600-606
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• 2007

Livestock wastewater containing concentrated organic matters and nutrients has been known as one of the major pollutants. It is difficult to apply the conventional activated sludge process to treat livestock wastewater because of high Non-biodegradable (NBD) matter and ammonia. The objectives of this study are to remove NBD matters including aromatic compounds and ammonia in livestock wastewater using Coagulation-Fenton oxidation-Zeolite (CFZ) processes and ascertain applicable feasibility in the field through pilot plant experiment. NBD matters and color remained in the treated water were removed over 92% by Fenton oxidation as the second treatment process. Ammonia was removed by over 99.5% in the zeolite ion exchange process as the last treatment method. From $UV_{254}$, $E_2/E_3$ ratio and GC/MS analyses of treated water at each process, the aromatic compound was converted to aliphatic and aromaticity was decreased. In pilot scale test, organics and ammonia removal efficiencies were not much different from the result of lab-scale test at various operation conditions. Furthermore, reaction time and dosage of Fenton reagent in pilot scale experiment reduced by 40 min and 50% rather than in lab-scale test. $BOD_5$, $COD_{Mn}$, SS, T-N and T-P of treated water in the pilot-scale experiment also met the effluent standards.

• Bulletin of the Korean Chemical Society
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• 제35권1호
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• pp.243-249
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• 2014

Three single crystals of fully dehydrated $Co^{2+}$-exchanged zeolite Y (Si/Al = 1.56) were prepared by the exchange of $Na_{75}$-Y ($|Na_{75}|[Si_{117}Al_{75}O_{384}]$-FAU) with aqueous streams 0.05 M in $Co(NO_3)_2$, pH = 5.1, at 294 K for 6 h, 12 h, and 18 h, respectively, followed by vacuum dehydration at 673 K. Their single-crystal structures were determined by synchrotron X-ray diffraction techniques in the cubic space group Fd3m at 100(1) K. They were refined to the final error indices $R_1/wR_2$ = 0.0437/0.1165, 0.0450/0.1228, and 0.0469/0.1278, respectively. Their unit-cell formulas are $|Co_{29.1}Na_{11.8}H_{5.0}|[Si_{117}Al_{75}O_{384}]$-FAU, $|Co_{29.8}Na_{11.0}H_{4.4}|[Si_{117}Al_{75}O_{384}]$-FAU, and $|Co_{30.3}Na_{9.5}H_{4.9}|[Si_{117}Al_{75}O_{384}]$-FAU, respectively. In all three crystals, $Co^{2+}$ ions occupy sites I, I' and II; $Na^+$ ions are also at site II. The tendency of $Co^{2+}$ exchange slightly increases with increasing contact time as $Na^+$ content and the unit cell constant of the zeolite framework decrease.

• 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.