• Korean Chemical Engineering Research
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• v.48 no.1
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• pp.80-87
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• 2010

Lignite of low rank coal and petroleum coke of high sulfur content can be high potential energy sources for coal gasification process because of their plentiful supply. The kinetic study of steam gasification has been performed in an atmospheric thermobalance with wood chip, lignite, bituminous, anthracite, pet-coke. The effects of gasification temperature($600{\sim}850^{\circ}C$) and partial pressure of steam(30~90 kPa) on the gasification rate have been investigated. The modified volumetric reaction model was applied to the experimental data to describe the behavior of carbon conversion and to evaluate the needed kinetic parameters. Lignite and wood chip with high volatile content showed high average gasification rates comparing to other fuel and thus they might be proper fuel for gasification processes. The activation energies for wood chip, lignite, bituminous, anthracite, and pet-coke through Arrhenius plot were found to be 260.3, 167.9, 134.6, 82.2, 168.9 kJ/mol, respectively. The expression of apparent reaction rates for steam gasification of various chars have been proposed as basic information for the design of coal gasification processes.

• Journal of Korean Society of Environmental Engineers
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• v.38 no.9
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• pp.513-520
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• 2016

It is well known that volatile compounds including disinfection by-products as well as emissive dissolved gas in water can be removed effectively by air stripping. The micro-bubbles of flotation unit are so tiny as microns while the diameter of fine bubbles applied to air stripping is ranged from hundreds to thousands of micrometer. Therefore, the micro-bubbles in flotation can supply very wide specific surface area to transfer volatile matters through gas-liquid boundary. In addition, long emission time also can be gained to emit the volatile compound owing to the slow rise velocity of micro-bubbles in the flotation tank. There was a significant difference of the THMs species removal efficiency between air stripping and flotation experiments in this study. Moreover, the results of comparative experiments on the removal characteristics of THMs between air stripping and flotation revealed that the mass transfer coefficient, $K_La$ showed obvious differences. To overcome the limit of low removal efficiency of dissolved volatile compounds such as THMs in flotation process, the operation range of bubble volume concentration is required to higher than the operation condition of conventional particle separation.

• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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• 2010.06a
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• pp.257-257
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• 2010

최근 저항 변화 메모리는 종래의 비휘발성 기억소자인 Flash memory보다 access time(writing)이 105배 이상 빠르고, DRAM과 같이 2~5 V 이하의 낮은 전압 특성 및 간단한 제조 공정 등으로 차세대 비휘발성 메모리 소자로 주목 받고 있지만, 여전히 소자의 Endurance 및 Retention 특성 등의 신뢰성 문제를 해결해야 할 과제로 안고 있다. 이러한 문제점들을 해결하기 위해 페로브스카이트계 산화물 또는 이원 산화물 등의 다양한 저항 변화 물질에 대한 연구가 진행되고 있다. 하지만, 현재 주로 연구되고 있는 금속 산화물계 물질들은 그 제조 공정상 산소에 의한 다수의 산소 디펙트 형성과 제작 시 쉽게 발생할 수 있는 표면 오염의 문제점을 안고 있다. 본 연구는 기존의 금속 산화물계 박막의 제조 공정에서 발생하는 문제점을 해결하기 위해 질화물계 박막을 저항변화 물질로 도입함으로써, 기존의 저항 변화 물질의 장점인 간단한 공정 및 저전압/고속 동작 특성을 동일하게 유지 할 뿐 아니라, 그 제조 공정상 발생하는 다수의 산소 디펙트와 표면 오염의 문제를 해결함으로써, 보다 고효율을 가지며 재현성이 우수한 메모리 소자를 구현 하고자 한다 [1, 2]. 본 연구를 위해 Pt/AlN/Pt 구조의 Metal/Insulator/Metal(MIM) 저항 변화 메모리를 제작 하였다. 최적의 저항 변화 특성 조건을 확인하기 위해 70~200nm까지 두께 구분과 N2 가스 분위기의 열처리 온도를 $200{\sim}600^{\circ}C$까지 진행 하였다. 본 소자의 저항 변화 특성 실험은 Keithley 4200-SCS을 이용하여 진행 하였다. 실험 결과, AlN의 최적의 두께 및 열처리 온도 조건은 130nm/$500^{\circ}C$였으며, 안정적인 unipolar 저항 변화 특성을 확인 활 수 있었다.

• Clean Technology
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• v.28 no.4
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• pp.285-292
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• 2022

Adsorption tower systems based on activated carbon adsorption towers have mainly been employed to reduce the emission of volatile organic compounds (VOCs), a major cause of air pollution. However, the activated carbon currently used in these systems has a short lifespan and thus requires frequent replacement. An approach to overcome this shortcoming could be to develop metal oxide photocatalysis-activated carbon composites capable of degrading VOCs by simultaneously utilizing photocatalytic activation and powerful adsorption by activated carbon. TiO₂ has primarily been used as a metal oxide photocatalyst, but it has low economic efficiency due to its high cost. In this study, ZnO particles were synthesized as a photocatalyst due to their relatively low cost. Silver nanoparticles (Ag NPs) were deposited on the ZnO surface to compensate for the photocatalytic deactivation that arises from the wide band gap of ZnO. A microfluidic process was used to synthesize ZnO particles and Ag NPs in separate reactors and the solutions were continuously supplied with a pack bed reactor loaded with activated carbon powder. This microfluidic-assisted pack bed reactor efficiently prepared a Ag-ZnO-activated carbon composite for VOC removal. Analysis confirmed that Ag-ZnO photocatalytic particles were successfully deposited on the surface of the activated carbon. Conducting a toluene gasbag test and adsorption breakpoint test demonstrated that the composite had a more efficient removal performance than pure activated carbon. The process proposed in this study efficiently produces photocatalysis-activated carbon composites and may offer the potential for scalable production of VOC removal composites.

• Journal of Energy Engineering
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• v.11 no.3
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• pp.269-275
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• 2002

Experimental studies are carried out to find the behavior of sulfur compounds which are evolved during high temperature pyrolysis of coals at the smelting reduction process for iron ore. Three kinds of bituminous coals, such as Hunter & Mt. Thorley (Australia), and Ensham (South Africa) are used. And forms of sulfur compound and their amounts are analyzed at the temperature ranges of 800~110$0^{\circ}C$. Then H$_2$S is the major gas, but CS$_2$ and COS are minor gases. Sulfur compounds in three coals are distributed into the volatiles (gas & tar) and coal char as the ratio of approximately 50%：50%, respectively.

• 한국가스학회:학술대회논문집
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• no.5
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• pp.189-194
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• 2002

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2014.11a
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• pp.37-37
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• 2014

유증기 처리 설비에서 발생하는 황화합물의 황산화 현상에 따른 부식손상은 설비의 안전운영 및 유지보수 공정에 영향을 미치는 주요 원인이며, 이에 대한 대책이 필요한 실정이다. 본 연구에서는 실제 유증기 가스 및 설비공정 상에서 발생되는 침출수를 채취하여 각각의 성상을 분석하고 부식을 일으킬 수 있는 황산화 현상에 대한 연구를 수행하였다. 또한, 발생 유증기의 액화에 따른 침출수의 배관부식 영향성을 확인하기 위하여 배관용 강관재료에 대한 무게감량시험 및 전기화학시험을 통해 침출수 pH 조건에 따른 부식경향성을 평가함으로써 유증기 처리설비의 부식방지 대안을 제시하고자 한다.

• Proceedings of the Korean Institute of Electrical and Electronic Material Engineers Conference
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• 2007.11a
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• pp.140-141
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• 2007

반도체 소자의 공정에 있어서 device scaling으로 인한 고유전 게이트 산화막 (high-k dielectics thin film)의 공정 개발 확보 방안이 필요하다. 본 논문에서는 유도결합 플라즈마를 이용하여 고유전율 박막을 식각하였다. CF4, SF6 등의 가스에서 금속-F, 금속-S 결합의 낮은 휘발성으로 인하여 시료 표면에 잔류하여 낮은 식각률을 보이며 측벽 잔류물을 형성하였으며, HBr, Cl 기반 플라즈마에서 금속-Br, 금속-Cl 결합은 시료 표면으로부터 탈착이 용이하여 효과적인 식각이 이루어짐을 확인할 수 있었다.

• Journal of Korea Soil Environment Society
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• v.4 no.3
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• pp.3-15
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• 1999

This paper includes the basic experimental results performed for developing an innovative and technologically feasible process wherein gaseous ozone, a powerful oxidant. is injected directly into vadose zone by which in-situ chemical degradation of semi- or, non-volatile petroleum product such as diesel fuel is derived. As ozone gas injected continuously(50mL/min, 119.0$\pm$6.1mg/L) into soil packed columns artificially contaminated with diesel fuel(initial concentration 1,485mg-DRO/kg/soil), the removal rates at the inlet and outlet point of 14hrs-operated column are 87.9% and 100.0%, respectively. On the other hand, soil vapor extraction system showed less than 30% of removal rates of residual diesel both at the inlet and outlet samples under the same experimental conditions which confirms the limited treatability of SVE in diesel contaminated soil.

• Fire Science and Engineering
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• v.29 no.6
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• pp.65-70
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• 2015

This research examines the removal efficiency of benzene, toluene, xylene (BTX) and total volatile organic compounds (TVOCs) by flowing VOCs, which are generated at a petrochemical complex in the Ulsan area, in a sliding arc plasma (SAP) reactor. The SAP reactor process is composed of 5 steps and the analysis was conducted using a BTX detector and TVOC measuring instrument. The removal efficiency of BTX was better at high concentration than at low concentration and the emitted TVOC concentration increased in later steps of the reactor. In addition, the removal efficiency improved, as the flow velocity increased. The maximum permissible concentration of TVOCs in the first step was about 481 ppm and showed over 94.83% efficiency when it was operated in the 2nd step at concentrations beyond 481 ppm. Therefore, there are many factors for improving the removal efficiency of SAP reactors at low concentration and measures should be prepared according to the application method for the various types of industrial reactors.