• Journal of Soil and Groundwater Environment
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• v.11 no.5
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• pp.35-42
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• 2006

The following results were obtained in the reductive degradation of hexachloroethane (HCA), and surface characteristics by using iron sulfide ($FeS,\;FeS_{2}$) mediators. HCA was degraded to pentachloroethane (PCA), tetrachloroethylene(PCE), trichloroethylene(TCE) and cis-l,2-dichloroethylene (cis-1,2-DCE) by complicated pathways such as hydrogenolysis, dehaloelimination and dehydrohalogenation. FeS had more rapid degradation rates of organic solvent than $FeS_{2}$. In liquidsolid reaction, the reaction rates of organic solvents were investigated to explain surface characteristics of FeS and $FeS_{2}$.. To determine surface characteristics of FeS and $FeS_{2}$, the specific surface area and surface potential of each mineral was determined and the hydrophilic site ($N_{s}$) was calculated. The specific surface area ($107.0470m^{2}/g\;and\;92.6374m^{2}/g$) and the $pH_{ZPC}$ of minerals ($FeS\;PH_{ZPC}=7.42,\;FeS_{2},\;PH_{ZPC}=7.80$) were measured. The results showed that the Ns of FeS and $FeS_{2}$ were $0.053\;site/mm^{2}\;and\;0.205\;site/mm^{2}$, respectively. $FeS_{2}$ had more hydrophilic surface than FeS. In other words, FeS have more hydrophobic surface site than $FeS_{2}$.

• Applied Chemistry for Engineering
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• v.16 no.5
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• pp.628-634
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• 2005

Zirconia-alumina polymer precursor was prepared from zirconium acetylacetonate (ZA). paluminium nitrate (AN), polyethylene glycol (PEG), and ethyl alcohol via an organic-inorganic solution technique. The thermal properties and viscosity of the polymer precursor were measured by differential scanning calorimetry (DSC), thermograbimetric analyzer (TGA), and dynamic viscometer. The vigorous exothermic reaction with volume expansion occurred at $140^{\circ}C$. The volume expansion was caused by abrupt decomposition of the organic group in metal compounds and the metal ions-PEG reaction. The evidences for these reactions were confirmed by FT-IR and $^{13}C$ solid NMR results. The peak intensity at N-O, O-H and C=C decreased with increasing temperature. This indicated that the decomposition of metal compounds and the metal ions-PEG reaction occurred during the vigorous exothermic reaction. At $800^{\circ}C$ for 2 h, the porous powders transformed to the crystalline $ZrO_2-Al_2O_3$ composites.

• 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$^{\circ}C$.

• Fire Science and Engineering
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• v.27 no.6
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• pp.64-69
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• 2013

The Numerical simulation was performed on the flow field around the two-dimensional rectangular bluff body in order to simulate an engine nacelle fire and to complement the previous experimental results of the bluff body stabilized flames. Fire Dynamic Simulator (FDS) based on the Direct Numerical Simulation (DNS) was employed to clarify the characteristics of reacting flow around bluff body. The overall reaction was considered and the constant for reaction was determined from flame extinction limits of experimental results. The air used atmosphere and the fuel used methane. For both fuel ejection configurations against an oxidizer stream, the flame stability and flame mode were affected mainly by vortex structure near bluff body. In the coflow configuration, air velocity at the flame extinction limit are increased with fuel velocity, which is comparable to the experiment results. Comparing with the isothermal flow field, the reacting flow produces a weak and small recirculation zone, which is result in the reductions of density and momentum due to temperature increase by reaction in the wake zone.

• Journal of Korean Society of Environmental Engineers
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• v.32 no.11
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• pp.1046-1053
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• 2010

The objective of this study was to investigate the pyrolytic reaction characteristics of a mixed fuel of municipal solid wastes and low-grade anthracite. The reaction variables are pyrolysis condition of mixing ratio, reaction temperature, temperature increase rate. As a result, the optimum mixing ratio was 20 wt.% low-grade anthracite in MSW, which maintains for the low heating value over 3,500 kcal/kg on pyrolysis. The most high reaction velocity constant was shown at $700^{\circ}C$. Also, under the all experimental condition, the reaction velocity constant increased linearly as temperature rate increase, but pyrolysis has to be considered electric power cost and yield of char at lower temperature rate.

• Applied Chemistry for Engineering
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• v.18 no.5
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• pp.511-515
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• 2007

The yield of oil was rapidly increased at $440^{\circ}C$ compared to $400^{\circ}C$ and $420^{\circ}C$ when the isothermal pyrolysis of waste ship lubricating oil was carried out in tubular type reactor, and pyrolysis was almost finished within 30 min. The yield of gas was decreased depending on the reaction temperature in which that of solid was not much changed. Pyrolysis experiments of waste ship lubricating oil were carried out with used ZSM-5 produced from a petrochemical process. The yield of gas was highly increased in the case of used ZSM-5 and fresh ZSM-5 compared to the case without catalyst. The produced oil and gas were almost constant for fresh ZSM-5 and used ZSM-5 at the same reaction temperature. In the reaction temperature $400{\sim}440^{\circ}C$, the selectivity of $C_5-C_{11}$ was two times higher with fresh ZSM-5 and used ZSM-5 than the case without catalyst.

• Korean Chemical Engineering Research
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• v.49 no.6
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• pp.752-757
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• 2011

The effects of reaction temperature, reactant concentration, pH of solution and mixing order of reactants on the particle shape and size distribution of zinc oxide were investigated in the preparation of zinc oxide from ammonium hydroxide and zinc acetate by the method of aqueous hydrothermal precipitation method, and the photocatalytic ability of zinc oxide synthesized was measured from the degradation of tartrazine under UV irradiation. The average particle size was increased with pH of solution but decreased with zinc acetate concentration and reaction temperature. The optimum condition for the synthesis of minimum sized zinc oxide was pH 11.2, concentration of zinc acetate 0.6 M and reaction temperature $90^{\circ}C$, and its average particle size was 3.133 ${\mu}$m. 97% of tartrazine was degraded by zinc oxide in sixty minutes.

• Proceedings of the Materials Research Society of Korea Conference
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• 2009.05a
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• pp.39.1-39.1
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• 2009

본 실험은 연성과 광 투명도가 뛰어난 아크릴 (PMMA) 과 폴리카보네이트 (Polycabonate) 기판의 축전 결합형 플라즈마 (CCP) 건식 식각 연구에 관한 것이다. 특히 식각 반응기 내부의 압력 변화에 따른 두 기판의 건식 식각 특성 분석에 초점을 맞추었다. 실험에 사용된 기판은 두께 1mm의 아크릴 (PMMA) 과 폴리카보네이트 (Polycabonate)를 $1.5\times1.5\;cm^2$로 절단하여 Photo-lithography 공정을 통하여 감광제 (Photo-resist)로 패턴하였다. 식각 반응기 내부에 패턴 된 아크릴(PMMA) 과 폴리카보네이트 (Polycabonate)를 넣은 후 반응기 내부 진공 상태로 만들었다. 그 후 5 sccm $O_2$ 가스를 유량조절기 (Mass flow controller)를 통하여 식각 반응기 내부로 유입하여 실험을 하였다. 이때 식각 공정 변수는 식각 반응기 내부 압력과 샘플 척 파워이다. 특성평가 항목은 식각 후 기판 (Substrate)의 식각율 (Etch rate), 식각 선택비 (Selectivity) 그리고 기판 표면 거칠기 (RMS roughness)이다. 실험 결과는 표면 단차 분석기(Surface profiler)를 이용하여 기판 (Substrate)의 표면을 분석 하였다. 또한 OES (Optical Emission Spectroscopy) 를 이용하여 식각 중 내부 플라즈마의 상태를 분석하였다. 본 실험 결과에 따르면 5 sccm $O_2$ 가스와 100 W 척 파워를 고정한 후 반응기 내부의 압력을 25 mTorr에서 180 mTorr까지 변화시켜 실험한 결과 40 mTorr의 반응기 내부 압력에서 실험 자료 중 가장 높은 식각율로 아크릴 (PMMA)은 $0.46\;{\mu}m/min$, 폴리카보네이트 (Polycabonate)는 $0.28\;{\mu}m/min$의 결과를 얻었다. 또한 이 자료를 바탕으로 5 sccm $O_2$ 가스와 반응기 내부 압력을 40 mTorr로 고정시키고 RIE 척 파워를 25 W에서 150 W로 증가시켰을 때 아크릴 (PMMA)의 식각율은 $0.15\;{\mu}m/min$에서 $0.72\;{\mu}m/min$까지 증가하였고, 폴리카보네이트 (Polycabonate) 의 식각율은 $0.1\;{\mu}m/min$에서 $0.36\;{\mu}m/min$까지 증가하였다.

• Journal of the Mineralogical Society of Korea
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• v.31 no.4
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• pp.227-234
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• 2018

In this work, we have prepared the reactive media with the pyrophyllite based using ceramic extrusion process. The characteristics of pyrophyllite were analyzed using XRD, XRF, DSC-TGA and Zeta-potential analysis. The study of pyrophyllite based ceramic reactive media were conducted under various roasting temperature (500 to $1,300^{\circ}C$) conditions. With increasing the roasting temperature, strength was increased but BET surface area was decreased. Thermally treated pyrophyllite were analyzed by means of weight loss and structural changes as detected by using XRD, DSC-TGA and SEM analysis. Pyrophyllite primarily transforms to pyrophyllite dehydroxylate after roasting at $1,000^{\circ}C$. Pyrophyllite dehydroxylate transforms to mullite and cristobalite at $1,300^{\circ}C$. This study demonstrates that pyrophyllite could be used as a reactive media for ceramic support layers from Permeable Reactive Barriers.

• Korean Journal of Materials Research
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• v.6 no.1
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• pp.106-115
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• 1996

본 연구에서는 PET(PentaEthoxy Tanatalum:Ta(OC2H5)5) 유기금속 화합물 전구체를 사용하여 차세대 초고집적회로 제조시 고유전체 물질로 유망한 Ta2O5 박막을 열화학증착 방법에 의하여 증착하였다. 본 증착실험을 통하여 여러 가지 운속기체, 기판온도, 반응압력 등의 공정변수가 층덮힘에 미치는 영향을 고찰하였으며 Monte Carlo 전산모사 결과와 기판온도 변화에 따른 층덮힘 패턴의 변화에 대한 실험결과를 비교하여 부착계수를 산출하였다. 운송기체로는 N2, Ar, He을 바꿔가며 실험하였으며 He>N2>Artns으로 층덮힘이 양호한 것으로 나타났다. 이는 운송기체의 종류에 따라 운동량 확산도, 열 확산도, 물질 확산도 등의 이동현상 특성값들이 다르기 때문이라 생각된다. 기판온도의 증가는 운송기체의 종류에 관계없이 층덮힘을 악화시켰으며 도랑내부에서의 Knudsen 확산과 표면반응물의 탈착에 비해 표면반응이 보다 지배적인 역할을 담당함을 알 수 있었다. 또한 질소를 운송기체로 사용한 경우에 부착계수의 겉보기 활성화 에너지는 15.9Kcal/mol로 나타났다. 그리고 3Torr 이하에서 반응압력이 증가하는 반응압력이 증가하는 경우에는 물질 확산도의 감소 효과 때문에 층덮힘이 악화되었다. 본 연구결과 3Torr, 35$0^{\circ}C$에서 He 운송기체를 이용한 경우가 가장 우수한 층덮힘을 얻을 수 있는 최적 공정 조건임을 알 수 있었다.