Tungsten disulfide (WS2) nanosheets have attracted considerable attention because of their unique optical and electrical properties. Several methods for fabrication of WS2 nanosheets have been developed. However, methods for mass production of high-quality WS2 nanosheets remain challenging. In this study, WS2 nanosheets were fabricated using mechano-chemical ball milling based on the synergetic effects of chemical intercalation and mechanical exfoliation. The ball-milling time was set as a variable for the optimized fabricating process of WS2 nanosheets. Under the optimized conditions, the WS2 nanosheets had lateral sizes of 500–600 nm with either a monolayer or bilayer. They also exhibited high crystallinity in the 2H semiconducting phase. Thus, the proposed method can be applied to the exfoliation of other transition metal dichalcogenides using suitable chemical intercalants. It can also be used with highperformance WS2-based photodiodes and transistors used in practical semiconductor applications.

In this study, (GaN)1-x(ZnO)x solid solution nanoparticles with a high zinc content are prepared by ultrasonic spray pyrolysis and subsequent nitridation. The structure and morphology of the samples are investigated by X-ray diffraction (XRD), field-emission scanning electron microscopy, and energy-dispersive X-ray spectroscopy. The characterization results show a phase transition from the Zn and Ga-based oxides (ZnO or ZnGa2O4) to a (GaN)1-x (ZnO)x solid solution under an NH3 atmosphere. The effect of the precursor solution concentration and nitridation temperature on the final products are systematically investigated to obtain (GaN)1-x(ZnO)x nanoparticles with a high Zn concentration. It is confirmed that the powder synthesized from the solution in which the ratio of Zn and Ga was set to 0.8:0.2, as the initial precursor composition was composed of about 0.8-mole fraction of Zn, similar to the initially set one, through nitriding treatment at 700oC. Besides, the synthesized nanoparticles exhibited the typical XRD pattern of (GaN)1-x(ZnO)x, and a strong absorption of visible light with a bandgap energy of approximately 2.78 eV, confirming their potential use as a hydrogen production photocatalyst.

3 mol% yttria-doped stabilized zirconia (3YSZ) is synthesized by a solvothermal process, and its characteristics are investigated using various methods. Also, the dispersibility of synthesized 3YSZ nanoparticles is observed with the species of surface modifier. The 3YSZ nano sol prepared with an optimum condition is employed in prism coating and its properties are evaluated. The synthesized 3YSZ nanoparticles show a globular shape with about 10 to 20 nm crystallite size. The mixed phases with the nano sol show a high specific surface of 178 m2/g. The prism sheet coated with the 3YSZ nano sol present an excellent refractive index, transmittance, and luminance; refractive index is 1.603, transmittance is 90.2 %, and luminance of coating film is improved by 5.9 % compared to that of the film without 3YSZ nano sol. It is verified that the surface modified 3YSZ is suitable as the prism sheet for optical displays.

In this work, TiO2 3D nanostructures (TF30) were prepared via a facile wet chemical process using ammonium hexafluorotitanate. The synthesized 3D TiO2 nanostructures exhibited well-defined crystalline and hierarchical structures assembled from TiO2 nanorods with different thicknesses and diameters, which comprised numerous small beads. Moreover, the maximum specific surface area of TiO2 3D nanostructures was observed to be 191 m2g-1, with concentration of F ions on the surface being 2 at%. The TiO2 3D nanostructures were tested as photocatalysts under UV irradiation using Rhodamine B solution in order to determine their photocatalytic performance. The TiO2 3D nanostructures showed a higher photocatalytic activity than that of the other TiO2 samples, which was likely associated with the combined effects of a high crystallinity, unique features of the hierarchical structure, a high specific surface area, and the advantage of adsorbing F ions.

A facile one-pot wet chemical process to prepare pure anatase TiO2 hollow structures using ammonium hexafluorotitanate as a precursor is developed. By defining the formic acid ratio, we fabricate TiO2 hollow structures containing fluorine on the surface. The TiO2 hollow sphere is composed of an anatase phase containing fluorine by various analytical techniques. A possible formation mechanism for the obtained hollow samples by self-transformation and Ostwald ripening is proposed. The TiO2 hollow structures containing fluorine exhibits 1.2 - 2.7 times higher performance than their counterparts in photocatalytic activity. The enhanced photocatalytic activity of the TiO2 hollow structures is attributed to the combined effects of high crystallinity, specific surface area (62 m2g-1), and the advantage of surface fluorine ions (at 8%) having strong electron-withdrawing ability of the surface ≡ Ti-F groups reduces the recombination of photogenerated electrons and holes.

화학물질 취급공정에서 발생하는 화학사고를 예방하기 위해 기본적으로 요구되는 위험성 분석 (Risk Analysis)시 공정의 특성을 잘 반영하는 것이 매우 중요하다. 본 연구에서는 CFD (computational fluid dynamics) 언어를 활용하여 화학공장의 고위험 공정을 대상으로 신뢰성 있는 사고 피해 결과를 분석하고 안전확보 방안을 제시하였다. 이를 위한 방법론적 사례로 화학공장의 RHDS (잔사유수첨탈황공정) 공정을 대상으로 실제공정의 운전조건, 설비 및 장치의 형태와 밀집도, 대기상태, 바람의 영향 등 여러 복합적 변수를 고려하여 FEA (Finite Element Analysis)와 CFD 시뮬레이션을 수행 하여 확산, 폭발 시뮬레이션을 수행하였으며, 3D Scanning 기술, 누출공 크기 산정, 누출량 산정을 위한 CFD 적용 가능성을 검토하였다.

In this study, using a wet chemical process, we evaluate the effectiveness of different solution concentrations in removing layers from a solar cell, which is necessary for recovery of high-purity silicon . A 4-step wet etching process is applied to a 6-inch back surface field(BSF) solar cell. The metal electrode is removed in the first and second steps of the process, and the anti-reflection coating(ARC) is removed in the third step. In the fourth step, high purity silicon is recovered by simultaneously removing the emitter and the BSF layer from the solar cell. It is confirmed by inductively coupled plasma mass spectroscopy(ICP-MS) and secondary ion mass spectroscopy(SIMS) analyses that the effectiveness of layer removal increases with increasing chemical concentrations. The purity of silicon recovered through the process, using the optimal concentration for each process, is analyzed using inductively coupled plasma atomic emission spectroscopy(ICP-AES). In addition, the silicon wafer is recovered through optimum etching conditions for silicon recovery, and the solar cell is remanufactured using this recovered silicon wafer. The efficiency of the remanufactured solar cell is very similar to that of a commercial wafer-based solar cell, and sufficient for use in the PV industry.

고리 1호기는 원전해체 계획에 따라 영구정지 이후 가능한 한 빠른 시일 내에 원자로냉각재계통의 화학제염을 수행할 계획으로, 계통제염 기술 확보를 위해 한수원에서는 2014년부터‘원전 해체설계를 위한 냉각재계통 및 기기제염 상용기술 개발’연구과제를 통해 화학제염기술을 개발하고 있다. 본 연구를 위해 Lab. 규모 계통제염 공정장치를 제작하였으며, 계통제염 대상의 주요재료인 STS304, 316, 410, Alloy600, SA508을 사용하여 화학제염 공정실험을 수행하였다. 화학제염 공정실험의 목적은 산화-환원공정의 최적시간, 최적제염제 및 공정횟수를 도출하기 위함이다. 화학제염 공정실험은 과망간산-옥살산 기반의 단위공정 및 연속공정 실험, 과망간산+질산-옥살산 기반의 연속공정 실험으로 나누어 수행하였다. 그 결과 단위공정실험을 통해 최적공정 시간인 산화공정 5시간, 환원공정 4시간을 도출하였으며, 연속공정실험을 통해 최적제 염제와 공정횟수를 도출하였다. 최적제염제는 산화제의 경우 200 mg·L-1 과망간산 + 200 mg·L-1 질산이고, 환원제는 2000 mg·L-1 옥살산이며, 공정횟수는 STS304와 SA508의 경우 2 cycle, Alloy600의 경우 3 cycle 이상 수행하는 것이 적절할 것 으로 평가되었다.

본 연구는 엽록소형광반응 분석을 이용하여 건조스트레스에 의한 공정육묘의 광화학적 활력을 분석하였다. 토마토와 오이 공정육묘를 8일 동안 건조스트레스 처리를 하였다. 엽록소형광반응 (OJIP)과 매개변수 분석을 통해 건조스트레스로 인한 작물의 광화학적 변동을 평가하였다. 엽록소 형광반응 (OJIP) 분석 결과, 토마토는 처리 후 5일부터 최대 형광량 (P)이 감소한 반면 J-I 단계에서는 엽록소 형광량이 증가하였다. 따라서 생리적 활력이 감소한 것을 알 수 있었다. 오이의 경우 처리 후 4일부터 최대 형광 (P) 및 변동 형광량 (FV)이 낮아지고 J-I 단계의 엽록소 형광 수치가 증가하였다. 엽록소 형광 매개변수 분석한 결과 토마토는 처리 후 5일부터 특히 ET2O/RC와 RE1O/RC가 감소하면서 광계II와 광계I의 전자전달효율이 유의적으로 낮아진 것으로 보인 반면 오이는 처리 후 4일부터 ET2O/RC와 PIABS가 상당히 변화하였다. 결론적으로 FV/FM, DIO/RC, ET2O/RC, RE1O/RC, PIABS, PITOTALABS 6개의 지표가 공정육묘의 건조스트레스를 판단하는 지표로 선정되었다. 건조스트레스지수 (DFI)를 통해 건조스트레스로 인한 작물별 건전성 평가를 하였고 오이의 경우 토마토에 비해 건조 저항성이 낮은 것으로 판단되었다.

Saline water electrolysis is an electrochemical process to produce valued chemicals by applying electric power. Perfluorinated sulfonic acid (PFSA) ionomers have been used as polymer electrolyte membrane (PEM) materials owing to their high sodium ion selectivity and barrier properties. However, sulfonic acid groups in PFSA ionomers are chemically decomposed under a basic catholyte condition, which makes the PEM materials lose their ionic selectivity and Faraday efficiency. In this study, double layered membranes were prepared by anchoring cross-linked hydrocarbon ionomers, as a protection layer to catholyte atmosphere, into the water channels, particularly, located at around the surface of a PFSA membrane. Here, each monomer results in the identical chemical architecture and different free volume content when polymerized.

우리는 정삼투 공정의 유도용질로서 잠재적인 활용 가능성을 확인하기 위해 식물화학물질인 tannic acid (TA)에 알칼리 염 처리한 alkali tannate 염 중 하나인 potassium tannate (TA-K)를 평가하였다. TA-K의 정삼투 특성과 회수 특성은 체계적으로 조사되었다. 정삼투 공정을 active layer facing feed solution (AL-FS) 방식으로 적용했을 때, TA-K 유도용액의 투수량은 TA 유도용액의 투수량 보다 훨씬 많은 반면, TA 유도용액의 투수량이 거의 확인되지 않았다. 100 mM 저농도에서 의 TA-K 유도용액의 삼투압(1,135 mOsmol/kg)은 NaCl 수용액의 삼투압(173 mOsmol/kg)의 약 6.5배로 확인되었다. 100 mM 농도의 TA-K의 투수량과 specific salt flux (6.14 LMH, 1.26 g/L)는 동일한 농도의 NaCl 유도용액의 투수량과 specific salt flux (2.46 LMH, 2.63 g/L)의 약 2.5배 및 0.5배로 각각 확인되었다. TA-K를 재사용하기 위해, 금속 이온 침전법을 이용 하여 TA-K유도용질을 침전시킨 후, membrane filtration을 이용하여 유도용질을 회수하였다. 이 연구는 식물화학물질을 정삼투 공정의 유도용질로서의 적용 가능성을 보여준다.

With increasing concerns of organic micropollutants, which are not removed by conventional wastewater treatment process, advanced oxidation processes (AOPs) are recently introduced. Among AOPs, electrochemical advanced oxidation processes (EAOPs) have advantages of simple operation and reasonable costs for construction and maintenance. However, low diffusion rate of pollutants from solution to electrode is regarded as a limitation. In this study, hollow fiber type of carbon nanotube (CHF) was fabricated and operated with flow through system to enhance mass transfer rate. The removal efficiency of BPA was achieved in following order: flow through, cross-flow, and batch methods. In addition, rate of removal in flow through system was significantly enhanced, comparing that of cross-flow operation.

In water treatment process using microfiltration membranes, manganese is a substance that causes inorganic membrane fouling. As a result of analysis on the operation data taken from I WTP(Water Treatment Plant), it was confirmed that the increase of TMP was very severe during the period of manganese inflow. The membrane fouling fastened the increase of TMP and shortened the service time of filtration or the cleaning cycle. The TMP of the membrane increased to the maximum of 2.13 kgf/cm2, but it was recovered to the initial level (0.17 kgf/cm2) by the 1st acid cleaning step. It was obvious that the main membrane fouling contaminants are due to inorganic substances. As a result of the analysis on the chemical waste, the concentrations of aluminum(146-164 mg/L) and manganese(110-126 mg/L) were very high. It is considered that aluminum was due to the residual unreacted during coagulation step as a pretreatment process. And manganese is thought to be due to the adsorption on the membrane surface as an adsorbate in feed water component during filtration step. For the efficient maintenance of the membrane filtration facilities, optimization of chemical concentration and CIP conditions is very important when finding the abnormal level of influent including foulants such as manganese.

Surface morphology and optical properties such as transmittance and haze effect of glass etched by physical and chemical etching processes were investigated. The physical etching process was carried out by pen type sandblasting process with 15~20 μm dia. of Al2O3 media; the chemical etching process was conducted using HF-based mixed etchant. Sandblasting was performed in terms of variables such as the distance of 8 cm between the gun nozzle and the glass substrate, the fixed air pressure of 0.5bar, and the constant speed control of the specimen stage. The chemical etching process was conducted with mixed etching solution prepared by combination of BHF (Buffered Hydrofluoric Acid), HCl, and distilled water. The morphology of the glass surface after sandblasting process displayed sharp collision vestiges with nonuniform shapes that could initiate fractures. The haze values of the sandblasted glass were quantitatively acceptable. However, based on visual observation, the desirable Anti-Glare effect was not achieved. On the other hand, irregularly shaped and sharp vestiges transformed into enlarged and smooth micro-spherical craters with the subsequent chemical etching process. The curvature of the spherical crater increased distinctly by 60 minutes and decreased gradually with increasing etching time. Further, the spherical craters with reduced curvature were uniformly distributed over the etched glass surface. The haze value increased sharply up to 55 % and the transmittance decreased by 90 % at 60 minutes of etching time. The ideal haze value range of 3~7 % and transmittance value range of above 90 % were achieved in the period of 240 to 720 minutes of etching time for the selected concentration of the chemical etchant.