• Proceedings of the KAIS Fall Conference
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• 2011.05a
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• pp.161-164
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• 2011

본 논문에서는 MBR 공정 유출수의 화학응집에 따른 특성을 알아보고자 A2O공정 하수처리수를 대상으로 막의 공극 크기와 약품 교반시간 및 응집 침전시간에 따른 인 제거 효율을 조사하였다. 막 여과 전후의 시료에 대한 응집실험결과 막 여과 전후의 응집제 투입에 따른 인 제거효율은 막 여과 전 90%와 비교했을 때 각각 74.5, 71.2, 62.6%로 최고 37.4%까지 큰 차이를 보였으며 이것은 막 여과로 인하여 시료 내 존재하는 콜로이드성 물질들의 입자 크기가 작아져 응집반응을 위한 응집핵 형성에 영향을 주었기 때문이며 막의 공극 크기가 작을수록 인 제거 효율도 감소하는 것으로 나타났다. 완속교반과 침전시간을 길게 할수록 인 제거 효율이 증가하였다. 침전시간이 10분일 경우는 인 제거 효율이 막 여과 후의 시료에 대해서 각각 45.3, 35.1, 52.0%로 인 제거가 상당히 불안정하였고 60분일 경우에는 각각 83.4, 85.1, 80.7%로 탁월한 인 제거가 일어난 것을 알 수 있었다.

• Applied Chemistry for Engineering
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• v.9 no.3
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• pp.407-412
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• 1998

This study was carried out to investigate the optimum leaching conditions for the sulfation and water leaching, and separation of cerium from rare earth elements in leached solution by acid-adjusting method. The optimum conditions for the sulfation and water leaching from bastnasite concentrates are that the equivalent ration of sulfuric acid to concentrates is 2.5, calcination temperature and time are $600^{\circ}C$ and 2 hrs respectively, and the pulp density in the water leaching is 9.1%. The yield of rare earth oxide is about 93% at the above condition. The process of recovery of cerium hydroxide from leached solution by acid-adjusting method was carried out as following steps. The first step is the oxidation of the solution at pH 5 by using twice the equivalent of $H_2O_2$ solution as an oxidant. The second step is the precipitation to obtain cerium complex salt and cerium hydroxide after lowering the solution to pH 2. The last step is the oxidation-precipitation by using equivalent of $H_2O_2$ solution. From these results, it was possible to prepare cerium hydroxide with the yield of 60% and the quality of 80%.

• Clean Technology
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• v.5 no.1
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• pp.20-29
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• 1999

In the treatment of Cu - and CN - contained wastewater by using Fenton oxidation-flocculation-precipitation, the optimal removal efficiencies of the cyanide and copper were investigated according to pH, reaction time, the molar ratio of cyanide and hydrogen peroxide and the mass ratio of ferrous sulfate and hydrogen peroxide for Fenton oxidation, and pH for hydroxide precipitation, respectively. As a result, the $CN^-$ removal efficiency in our experimental wastewater by the Fenton oxidation was 81.2%~99% at its optimal conditions of pH ranging from 3 to 5 and reaction time of 30 minutes. And the optimal dosage of hydrogen peroxide and ferrous sulfate was 214, $428mg/{\ell}$, 107, $161mg/{\ell}$, 214, $214mg/{\ell}$ and 520, $500mg/{\ell}$, respectively when the molar ratio of $Cu^{2+}$:CN is 2:1, 1:1, 1:2, 1:10, and was 900, $1050mg/{\ell}$ when the molar ratio of $Cu^+$: CN is 1:10. When the copper was precipitated by sodium hydroxide after Fenton oxidation, the copper removal efficiency in the wastewater at pH 7 was 98.92%, 98.52%, 92.46%, 90.6% and 95%, respectively.

• Journal of the Korean Graphic Arts Communication Society
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• v.16 no.2
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• pp.11-22
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• 1998

For the purpose of preparation of monodispersed spherical zinc oxide fine particles, an experimental research on the preparation of zinc oxide particles from zinc salts solutions by high temperature precipitation reaction was performed. Zinc oxide particles were precipitated from all the precipitation solutions tested if the precipitation temperature was higher than 60$^{\circ}$. As the precipitation temperature Increased until 80$^{\circ}$, the average particle diameter of zinc oxide particles decreased and the narrower particle size distribution were obtained. Spherical zinc oxide fine particles with relatively narrow particle size distribution were precipitated from the ZnSO$_4$ solutions with NaOH as precipitant. Final pH of precipitation solution had an effect on the amount of zinc oxide precipitated, but had no effect on the their particle size or size distribution.

• Journal of the Korean Chemical Society
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• v.24 no.1
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• pp.53-62
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• 1980

The present work is concerned with the studies on the production of PZT ceramics by newly developed mixing process, which tentatively named "precipitation mixing method", consists of precipitating lead carbontate in the presence of $TiO_2$ and/or $ZrO_2$. Mixtures of $PbCO_3$ and $TiO_2$ or $ZrO_2$ were compared with those obtained by ball-milling with special emphasis on the rate and mechanism of formation of lead titanate and lead zirconate. A possiblity for obtaining PZT ceramics by "precipitation mixing method" was established.

• Journal of the Mineralogical Society of Korea
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• v.14 no.1
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• pp.1-11
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• 2001

미국 메사추세츠 북중부에 산출되는 데본기 리틀톤층(Littleton Formation)의 남정석-십자석-석류석대에서 채취한 석류석 반상변정의 화학적 누대구조는 여러 번의 성장 단계를 경험했음을 보여준다. 석류석 반상변정들은 비대칭적이고 불규칙적인 Mn, Mg, Ca의 누대구조를 보인다. 조직대 경계부에서 석류석 성분들은 단면선에 따라 그 형태가 다르게 나타나고, $X_{Mn}$ 과 Fe/(Fe+Mg)비의 역전 누대구조는 석류석내의 내부엽리의 발달과 밀접한 관계를 보여준다. 이런 관찰 사항들은 석류석 누대구조가 석류석을 형성/소모시키는 반응뿐만 아니라, 용해작용과 침전작용과 관련된 기존의 미세구조에 의해 변화되었음을 의미한다. 화학적 그리고 조직적 잘림구조의 관계 그리고 저자가 제안한 석류석 성장모델은 석류석 누대구조가 엽리의 발달 동안 전단 응력대에서 일어나는 선택적 용해작용과 압축 운동대에서 발생하는 침전작용에 의해 조절되었음을 지시한다.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2014.11a
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• pp.89-90
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• 2014

인쇄회로기판 패턴도금 박리공정 중 발생하는 폐솔더 박리액은 주석, 구리, 철, 납 등 유가금속이 함유된 질산계 폐액이다. 본 연구에서는 이러한 폐솔더 박리액에서 질산과 유가금속을 체계적으로 회수하는 기술을 개발하고자 하였다. 먼저 폐액을 $80^{\circ}C$에서 3시간 정도 반응시켜 주석을 $SnO_2$ 상태로 90% 이상 회수가 가능하였다. 주석이 회수되고 구리, 철, 납만이 존재하는 질산계 폐솔더 박리액에서 확산투석을 이용하여 질산을 94% 이상 회수가 가능하였고 회수된 질산의 농도는 5.1 N 이었다. 질산을 추출한 폐액에서 침전제로 옥살산(Oxalic acid)을 사용하여 구리를 구리옥살레이트 상태로 침전시켜 타금속이온과 선택적으로 분리하였다. 마지막으로 폐액 중 용해되어있는 납을 $65^{\circ}C$이상에서 철 스크랩을 이용한 세멘테이션을 통하여 회수하였다.

• Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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• v.5 no.4
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• pp.273-281
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• 2007

Hyperalkaline groundwater formed by groundwater-cement components and its reaction with bedrock in a nuclear waste repository were simulated by geochemical modeling. The result of groundwater-cement components reaction showed that the pH of water was 13.3 and the precipitated minerals were Brucite, Katoite, Calcium Silicate Hydrate(CSH1.1), Ettringite, Hematite, and Portlandite. The result of interaction between such minerals and groundwater sampled in Gyeongju area also showed that the pH of groundwater reached 12.4. Interaction between such hyperalkaline groundwater and granite was simulated by kinetic model during $10^3$ years. This result showed that the final pH of groundwater reached 11.2 and the variation of pH was controlled by dissolution/precipitation of silicate and CSH minerals. Groundwater quality was also determined by dissolution/precipitation of silicate, CSH, oxide minerals. Our results show that geochemical modeling of long-term hyperalkaline groundwater and rock interaction can contribute to the safety assessment of engineered barrier by predicting geochemical condition in repository site.

• Economic and Environmental Geology
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• v.46 no.3
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• pp.221-234
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• 2013

Laboratory experiments for the reaction with supercritical $CO_2$ under the $CO_2$ sequestration condition were performed to investigate the mineralogical and geochemical weathering process of the sandstones and mudstones in the Pohang basin. To simulate the supercritical $CO_2$-rock-groundwater reaction, rock samples used in the experiment were pulverized and the high pressurized cell (200 ml of capacity) was filled with 100 ml of groundwater and 30 g of powdered rock samples. The void space of the high pressurized cell was saturated with the supercritical $CO_2$ and maintained at 100 bar and $50^{\circ}C$ for 60 days. The changes of mineralogical and geochemical properties of rocks were measured by using XRD (X-Ray Diffractometer) and BET (Brunauer-Emmett-Teller). Concentrations of dissolved cations in groundwater were also measured for 60 days of the supercritical $CO_2$-rock-groundwater reaction. Results of XRD analyses indicated that the proportion of plagioclase and K-feldspar in the sandstone decreased and the proportion of illite, pyrite and smectite increased during the reaction. In the case of mudstone, the proportion of illite and kaolinite and cabonate-fluorapatite increased during the reaction. Concentration of $Ca^{2+}$ and $Na^+$ dissolved in groundwater increased during the reaction, suggesting that calcite and feldspars of the sandstone and mudstone would be significantly dissolved when it contacts with supercritical $CO_2$ and groundwater at $CO_2$ sequestration sites in Pohang basin. The average specific surface area of sandstone and mudstone using BET analysis increased from $27.3m^2/g$ and $19.6m^2/g$ to $28.6m^2/g$ and $26.6m^2/g$, respectively, and the average size of micro scale void spaces for the sandstone and mudstone decreased over 60 days reaction, resulting in the increase of micro pore spaces of rocks by the dissolution. Results suggested that the injection of supercritical $CO_2$ in Pohang basin would affect the physical property change of rocks and also $CO_2$ storage capacity in Pohang basin.

• Resources Recycling
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• v.17 no.1
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• pp.38-42
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• 2008

This study was carried out to investigate the solubility of vanadium in ammoniacal solution and precipitation of $NH_4VO_3$ as a function of temperature and addition of ammonia salt. Higher solution temperature is required to get high solubility of vanadium and the vanadium concentration of solution was 16.8g/L at $90^{\circ}C$ with the solution of 20 g/L $(NH_4)_2CO_3$ and 2.5M $NH_4OH$. From this solution, vanadium could be precipitated up to 99.8% with adding 20 g/L $NH_4Cl$, 72 hours settling time at $25^{\circ}C$.