• Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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• 2001.04a
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• pp.34-37
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• 2001

폐수처리분야에 널리 사용되어 온 펜톤산화반응을 응용한 Fe$^{\circ}$/$H_2O$$_2$시스템을 이용하여 고농도 유류오염 미세호양(100$\mu\textrm{m}$이하)의 화학적 산화처리 실험을 수행하였다. 반응은 100$m\ell$, 삼각프라스크에 오염토양(5g)과 반응시약을 주입한 후 자석교반기를 이용하여 회분 식으로 진행하였으며 일정 시간(0, 1, 2, 4, 8, 24hr)별로 TPH를 측정하였다. 그리고 각 조건별 시간에 따른 반응특성을 살펴보았다. 일반적으로 알려진 펜톤산화반응의 수요 반응조건인 초기 pH /$H_2O$$_2$ 및 Fe$^{\circ}$의 주입농도, 그리고 초기 디젤오염농도의 조건을 변화하며 각 조건별 처리효과를 알아보았다. 본 연구결과에서 최적 pH조건은 3인 것으로 나타났으며, 분말철(Fe$^{\circ}$)과 $H_2O$$_2$의 주입농도를 증가함에 따라 오염토양의 TPH 제거효율도 비례적으로 향상되었다. 초기오염농도에 따른 최종 처리효율은 큰 차이가 없었으나. 고농도 오염일수록 제거된 디젤의 총량은 크게 나타나. 본 논문에서 제시한 방법이 고농도 오염토양일수록 더 큰 효과를 얻을 수 있음을 보여주었다. 대부분의 반응이 반응개시 후 약 8시간 이내에 이루어졌는데, 반응에 수반되는 pH 상승과 그에 따른 반응성의 저감효과를 일정 pH 조절에 의해 감소시킴으로써 반응성의 향상을 좀 더 높일 수 있을 것으로 판단된다. 결론적으로, Fe$^{\circ}$/$H_2O$$_2$시스템을 이용한 화학적 산화처리방법은 경제성과 처리성능에서 고농도 유류오염 미세토양의 효율적인 처리방안으로서 향후 적용 가능성이 높을 것으로 기대된다.

• Proceedings of the Korean Institute of Surface Engineering Conference
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• 2011.05a
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• pp.77-78
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• 2011

저비용, 고효율, 안정적 수급이 가능한 전력 에너지원이 요구되면서 석탄이 새로운 에너지원으로 급부상하게 됨에 따라 차세대 친환경 석탄화력 발전기술인 IGCC (Integrated Gasification Combined Cycle) 발전 시스템 의 개발이 필요하게 되었다. 석탄가스화 공정(IGCC: integrated coal gasification combined cycle)은 석탄을 가스화한 후 이를 이용하여 복합발전소를 운전하는 발전기술로서 석탄을 고온, 고압아래에서 수소와 일산화탄소를 주성분으로 한 합성가스로 전환한 뒤 합성가스 중에 포함 된 분진과 황 화합물 등 유해물질을 제거하고 천연가스와 유사한 수준으로 정제하여 전기를 생산하는 친환경 발전 기술이다.

• KSBB Journal
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• v.23 no.1
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• pp.83-89
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• 2008

Food wastewater derived from the three-stage methane fermentation system developed in this lab contained high concentration organic substances. The organic wastewater should be treated through advanced wastewater treatment system to satisfy the "Permissible Pollutant Discharge Standard of Korea". In order to treat the organic wastewater efficiently, several optimum operation conditions of a modified $UV/TiO_{2}$ photocatalytic system have been investigated. In the first process, wastewater was pre-treated with $FeCl_{3}$. The optimum pH and coagulant concentration were 4.0 and 2000mg/L, respectively. Through this process, 52.6% of CODcr was removed. The second process was $UV-TiO_{2}$ photocatalytic reaction. The optimum operation conditions for the system were as follows: UV lamp wavelength, 254 nm; wastewater temperature, $40^{\circ}C$; pH 8.0; and air flow rate, 40L/min, respectively. Through the above two combined processes, 69.7% of T-N and 70.9% of CODcr contained in the wastewater were removed.

• Journal of Life Science
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• v.13 no.6
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• pp.917-923
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• 2003

The present investigation was conducted to determine the chemical oxygen demand (COD) removal efficiency by Pseudomonas aeruginosa EMS1. The COD removal efficiency in the medium containing 1% metal working fluid (MWF) was 12% after cultivation of 4 days. The composition of optimum medium for the COD removal efficiency of 1% MWF by P. aeruginosa EMS1 were NH$_4$Cl 0.3%,$ K_2HPO_4\; 0.05%,\; KH_2PO_4\; 0.04%,\; MgSO_4.7H_2O\; 0.05%,\; CaCl_2.2H_2O 0.03%$ and $FeSO_4.7H_2O$ 0.04% at initial pH 7.0 and $30^{\circ}C$. Under this condition, the highest the COD removal efficiency was observed after 4 days.

• Korean Chemical Engineering Research
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• v.49 no.5
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• pp.530-534
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• 2011

The synthesis of dimethyl carbonate by liquid phase oxidative carbonylation of methanol was studied under batch reaction system. Reaction factors such as effect on various metals, anion containing in copper catalyst, temperature, carbon monoxide and oxygen molar ratio and copper content were investigated. In particular $CuCl_2{\cdot}2H_2O$ showed the excellent of the methanol conversion 65.2%, DMC selectivity 96.6% reaction condition under 1.0 g, $150^{\circ}C$, MeOH/CO/$O_2$=0.2/0.215/0.05 (molar ratio). $CuCl_2$ led to corrosion of the reactor. Thus, a new catalyst system using supports was investigated to resolve these corrosion problem. Influence on various supports were examined and copper catalyst supported on zeolite Y showed the most excellent activity on the formation of dimethyl carbonate. The amount of Fe dissolved during the reaction using ICP-AES (Inductively Coupled Plasma-Atomic Emission Spectrometer) was compared with catalysts, calcined Cu/zeolite Y showed the lower value below 5% than $CuCl_2-2H_2O$.

• Korean Chemical Engineering Research
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• v.44 no.3
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• pp.307-313
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• 2006

In order to improve the efficiency of methane steam reforming process, a part of the system which produces hydrogen from heavy hydrocarbon resources such as coal, we combined metal catalyst with CaO sorbent and fabricated catalyst/sorbent. To increase the porosity and the compressive strength of sorbent, carbon black and ${\alpha}-alumina$ were mixed with CaO powder during preparation. The effects of sorbent composition on the physical properties were investigated by SEM, TGA, BET, XRD, abrasion strength measuring device and adsorption-desorption instrument. Sorbent with 5 wt％ $Al_2O_3$ and 10 wt％ carbon black showed the best physical features with $7.61kg_f$ strength and 47％ $CO_2$ adsorption capability. Various metal catalysts such as Ni, Co and Fe were supported on the sorbent developed and 10 wt％ Ni/sorbent was selected for methane steam reforming process based on the result of reaction experiment. The reaction system using the catalyst/sorbent showed better $H_2$ productivity compared to the detached system with catalyst and sorbent, indicating the effectiveness of the system developed in this study.

• Journal of Energy Engineering
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• v.5 no.2
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• pp.123-130
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• 1996

Reduction, sulfidation, and regeneration reactions were performed using domestic and Australian iron ore in order to develop a desulfurizing sorbent for the high temperature desulfurization process that is one of major processes in the integrated coal gasification combined cycle (IGCC) system. A TGA (Thermogravimetric Analysis) reactor and a fixed-bed reactor were used. Some basic kinetic information was obtained from BET surface area measurements, SEM photos, cyclic reactions, reaction temperature changes and TGA curves of the sorbents. The rates of both desulfurization and regeneration increased with increasing reaction temperature in the range of 500-700$^{\circ}C$.

• Proceedings of the Korean Society of Dyers and Finishers Conference
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• 2012.03a
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• pp.85-85
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• 2012

천연염색은 독성과 환경오염이 적으며 합성염료로는 얻기 어려운 자연스러운 색감 등을 표현할 수 있는 장점에 비하여 염색과정 및 보관의 어려움, 재현성 부족, 낮은 염착량과 견뢰도, 염색과정에서 노동력이 많이 소비되어 대량생산의 어려움 등의 문제점으로 인해 아직 공업화되지 못하고 있다. 천연염료는 합성염료에 비해 색상이 차분하고 은은하며 변퇴색이 일어나도 안정된 색감을 나타낼 뿐 아니라 매염제에 의해 다양한 명도와 색상변화를 꾀할 수 있어 천연염색물에 대한 소비자의 수요가 최근 증가하고 있다. 본 연구에서는 천연염색 공정의 기계화를 통해 대량생산 및 재현성 확보가 가능한 100yd급 염색시스템을 설계 제작하고 천연염료인 소목을 이용하여, 면 및 견을 포함한 10종의 원단에 염액비(1:20), 매염제($FeSO_4{\cdot}7H_2O$)를 사용하여 염색 온도변화($20^{\circ}C{\sim}80^{\circ}C$)에 따른 원단별 염색특성을 평가하였다. 평가결과 세탁견뢰도는 온도가 증가할수록 대부분의 원단에서 견뢰도가 상승하였으며, 염색된 원단내의 색차(${\Delta}E$) 평가에서 대부분의 원단에서 1.0미만의 균염성을 나타내었다.