• 한국환경농학회지
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• 제24권3호
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• pp.232-237
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• 2005

This study was conducted to elucidate the effects of NaOH fusion treatment on Na-P1 zeolite synthesis from fly ash and to evaluate its optimal condition. NaOH fusion treatment of fly ash led to Na-P1 zeolite with shorter reaction time and higher quality compared that of simple hydrothermal method. Mixed zeolite phases of Na-P1 and hydroxy sodalite were formed by the fusion treatment below $450^{\circ}C$, whereas only Na-P1 zeolite was formed above $550^{\circ}C$. Ratio of NaOH/fly ash, reaction times, fusion temperature and solid/liquid ratio strongly affected the kind and crystallinity of the zeolite formed. The CEC of Na-P1 zeolite formed at the optimum reaction conditions of NaOH/fly ash ratio 0.9 and solid/liquid ratio $1/5.0{\sim}1/7.5$ after NaOH fusion treatment at $550^{\circ}C$ for 2 hours was about $398cmol^+kg^{-1}$ which was 40% higher than those of control products. Therefore, it is clear that NaOH fusion treatment of fly ash in open system could lead to Na-P1 zeolite with high purity.

• 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.

• 한국산학기술학회논문지
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• 제1권2호
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• pp.33-40
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• 2000

본 연구는 반도체 크린룸에서 VOC(volatile organic compound)과 수분을 제거하기 위한 흡착로타에 관한 것이다. 흡착로타는 세라믹 페이퍼 허니컴 기질에 NaX 제올라이트와 TS-1 제올라이트로 만들어졌다. NaX 제올라이트는 수열합성법으로 합성되어졌으며, NaX 제올라이트 결정(2∼3 ㎛)을 seed로 합성 조성에 3∼5 wt%까지 첨가하여 5 ㎛의 균일한 NaX 제올라이트를 성장시켰다. Seed의 첨가는 seed를 첨가하지 않은 합성용액과 비교하여 결정의 크기가 크며, 균일한 NaX 제올라이트 결정을 성공적으로 합성하였다. TS-1 제올라이트는 초기 반응액의 pH를 변화시켜 합성하였다. 반응물의 pH는 10.0에서 11.5 까지의 범위를 가지며, PH 10.4에서 큰 기공(8∼10 (equation omitted))을 가진 TS-1 제올라이트(ETS-10)가 합성되는 반면 pH가 11.5에서는 작은 기공 (3∼5 (equation omitted))을 갖는 TS-1 제올라이트(ETS-4)가 합성되었다.

• Applied Biological Chemistry
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• 제25권2호
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• pp.99-104
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• 1982

천연(天然) zeolite를 분리(分離)하여 동정(同定)한 후(後) $Na^+$로 포화시키고 3가지 농도의 NaCl용액 중(中)에서 P흡착현상(吸着現象)을 $P^{32}$ 동위원소(同位元素)를 이용(利用)하여 조사(調査)하였다. Na-zeolite에는 pH가 낮을수록, 반응시간(反應時間)이 길수록 또 시료량(試料量)이 많을수록 P흡착량(吸着量)이 증가(增加)됐으며 시료(試料)와 용액(溶液)의 비율(比率)이 작은 편이 단위중량당(單位重量當) 흡착량(吸着量)이 많았다. 전해질(電解質) 농도가 클수록 P의 흡착량(吸着量)이 늘었으며 최대흡착량(最大吸着量)은 1me/g 정도(程度)였으며 Na-zeolite의 ZPC는 pH 3.7 이하(以下)일 것으로 추정(推定)된다.

• 한국환경과학회지
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• 제20권10호
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• pp.1337-1345
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• 2011

The removal performances of divalent heavy metal ions ($Pb^{2+}$, $Cu^{2+}$, $Cd^{2+}$, $Sr^{2+}$ and $Mn^{2+}$) were studied using the Na-P1 zeolite synthesized from Jeju scoria in the batch and continuous fixed column reactor. The uptakes of heavy metal ions by synthetic Na-P1 zeolite decreased in the order of $Pb^{2+}$ > $Cu2^{2+}$ > $Cd^{2+}$ > $Sr^{2+}$ > $Mn^{2+}$ based on the selectivity of each ion to ionic exchange site of Na-P1 zeolite for single and mixed solutions in batch or continuous fixed column reactor. For mixed solution, each heavy metal ion uptake was lower than that in single solution, and especially the uptake for $Mn^{2+}$ decreased greatly. In batch reactor, the uptakes of heavy metal ions by synthetic Na-P1 zeolite were described by Freundlich or Langmuir equation, but they followed the former better than the latter. In continuous fixed column reactor, the maximum ion exchange capacity obtained for each of heavy metal ions, was about 90----- of that in batch reactor. The uptakes of heavy metal ions by synthetic Na-P1 zeolite increased with the increase of initial heavy metal concentration and solution pH, and the decrease of the amount and particle size of synthetic zeolite.

• 대한화학회지
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• 제17권1호
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• pp.47-52
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• 1973

우리나라 영일산 Bentonite를 0.5-6 N NaOH로 $70-90^{\circ}C$에서 $Na_2:SiO_2$의 비율로 $1:1{\sim}4:1$로 2-30일의 범위에서 처리하여 그 겨정성의 변화를 X선회절법으로 조사하였다. 그 결과 2N NaOH로 $70^{\circ}C$에서 Zeolite Species가 좋은 수율로 생성되었다. 그러나 NaOH의 농도가 더 크고 온도가 더 높으면 이 Zeolite는 Hydrozysodalite로 변한다. 이 결정 외에도 처리조건에 따라서는 raujasite, sodium A zeolite, mordemite등의 결정도 소량 생겼다.

• Environmental Sciences Bulletin of The Korean Environmental Sciences Society
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• 제1권2호
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• pp.167-175
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• 1997

This study was conducted for an efficient utilization of waste fly ash obtained from the power plant. Fly ash was used for synthesizing zeolite. Na-P1 zeolite could be easily synthesized from waste fly ash and showed the potential to remove heavy metal ions. The synthetic zeolite showed good adsorption property for heavy metal much better than raw fly ash and natural zeolites. Na-P1 exhibited the high adsorption efficiency with a maximum value of 260 Pb mg/g and strong affinity for $Pb^{2+}$ ion. The metal ion selectivity of Na-P1 was determined in a decreasing order : $Pb^{2+}>Cd^{2+}>Cu^{2+}>Zn^{2+}>Fe^{3+}$.

• 한국결정성장학회지
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• 제9권1호
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• pp.6-13
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• 1999

NaX zeolite 결정을 성장시키기 위하여 ${4.12{Na}_{2}O{\cdot}{Al}_{2}{O}_{3}{\cdot}3.5{SiO}_{2}{\cdot}593{H}_{2}O$의 몰비를 가진 모액에 합성된 NaX powder(1~2$\mu\textrm{m}$)를 seed를 첨가하였다. 그 결과 초기 혼합물에 seed를 첨가하므로 결정화 시간을 감소시킬수 있었으며, 결정의 크기도 감소하는 것으로 나타났다. 하지만 결정화 시간을 증가시키면 NaX zeolite 결정은 보다 안정한 NaP zeolite와 또 다른 상으로의 전이가 발생하였다. 본 연구에서 우리는 이러한 결과에 대해서 XRD, SEM, FT-IR과 BET을 이용하여 상세하게 연구하였다.

• 방사성폐기물학회지
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• 제20권1호
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• pp.1-12
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• 2022

Bentonite is the most probable candidate to be used as a buffer in a deep geological repository with high swelling properties, hydraulic conductivity, thermal conductivity, and radionuclide sorption ability. Among them, the radionuclide sorption ability prevents or delays the transport of radionuclides into the nearby environment when an accident occurs and the radionuclide leaks from the canister, so it needs to be strengthened in terms of long-term disposal safety. Here, we proposed a surface modification method in which some inorganic additives were added to form NaP zeolite on the surface of the bentonite yielded at Yeonil, South Korea. We confirmed that the NaP zeolite was well-formed on the bentonite surface, which also increased the sorption efficiency of Cs and Sr from groundwater conditions. Both NaP and NaX zeolite can be produced and we have demonstrated that the generation mechanism of NaX and NaP is due to the number of homogeneous/heterogeneous nucleation sites and the number of nutrients supplied from an aluminosilicate gel during the surface modification process. This study showed the potential of surface modification on bentonite to enhance the safety of deep geological radioactive waste repository by improving the radionuclide sorption ability of bentonite.

• 한국토양비료학회지
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• 제32권1호
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• pp.39-46
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• 1999

Fly ash를 이용(利用)한 zeolite성(性) 물질(物質)의 열수합성(熱水合成)에 있어서 반응재료(反應材料)의 초기구성성분(初期構成成分) 비율(比率)과 여러가지 반응조건(反應條件)이 반응생성물(反應生成物)의 CEC및 결정화도(結晶化度)에 미치는 영향(影響)과 최적반응조건(最適反應條件)을 조사(調査)하였다. $SiO_2/Al_2O_3$ 비율(比率)이 2.55이상(以上)에서는 Na-P1 zeolite가 생성(生成)되었으나, 2.25이하(以下)에서는 hydroxy sodalite가 생성(生成)되었다. 3N-NaOH, $SiO_2/Al_2O_3$ 비율(比率) 2.55, $Na_2O/Al_2O_3$ 비율(比率) 2.0, $103^{\circ}C$에서 12시간(時間) 처리(處理)한 반응생성물(反應生成物)의 CEC 가 $285cmol^+kg^{-1}$으로 다른 반응조건(反應條件)의 생성물(生成物)보다 높았으며, 결정화도(結晶化度)는 2N-NaOH, $SiO_2/Al_2O_3$ 비율(比率) 2.55 $Na_2O/Al_2O_3$ 비율(比率) 2.0, $103^{\circ}C$에서 12시간(時間) 처리(處理)한 반응생성물(反應生成物)이 45.1%로서 가장 높게 나타났다. 반응생성물(反應生成物)의 $SiO_2/Al_2O_3$ 비율(比率)은 fly ash 보다 낮았으며, ignition loss는 결품격자(結品格子) 내(內)의 흡착수(吸着水)에 의해 4.0%로 증가(增加)하였다. 반응생성물(反應生成物)의 XRD peak와 전자현미경사진(電子顯微鏡寫眞)으로 관찰(觀察)한 결과(結果) Na-P1 zeolite의 특징(特徵)을 나타내었다. Fly ash를 이용(利用)한 Na-P1 zeolite의 최적(最適) 열수합성조건(熱水合成條件)은 NaOH 농도(濃度) 2~3N, $SiO_2/Al_2O_3$, 2.55, $Na_2O/Al_2O_3$ 비율(比率) 1.5~2.0, 반응온도(反應溫度) $80{\sim}103^{\circ}C$, 반응시간(反應時間)은 12시간(時間) 이상(以上)으로 판단(判斷)된다.