• Applied Chemistry for Engineering
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• v.20 no.4
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• pp.381-385
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• 2009

A basic objective is the preparation and surface studies of supported molten salt catalysts because molten salts can stay as the liquid phase in the range of the ordinary reaction temperature. Many kinds of metal salt mixtures for the formation of molten salt phase are appliable but CuCl and KCl were selected in this study because Cu is considered catalytically reactive in many reactons. The loading of the molten salt was selected as 25 vol% of the total pore volume of ${\gamma}-alumina$ to provide reasonable exposed surface area. The surface structure of catalysts containing molten salts in the ${\gamma}-alumina$ was studied using scanning electron microscopy (SEM) and energy-dispersive spectroscopy (EDS). CuCl and KCl were added into the ${\gamma}-alumina$ using concentrated hydrochloric acid solution by the impregnation technique. The surfaces of the prepared catalysts before and after heat treatments were compared and they suggested that the heat treatment of catalysts helped the formation of molten-salt although the surface compositions of CuCl and KCl were not uniform.

• Journal of the Korean Applied Science and Technology
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• v.29 no.2
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• pp.193-198
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• 2012

The following results are from the test of semi-gel electrolyte to store energy efficiently and use advanced VRLA batteries by photovoltaic and wind power generation. Semi-Gel electrolyte with Silica 5% became Gel after 1 and half hour. It shows it is the most suitable time that the electrolyte can be absorbed into the separator and active material of plate to be gel. The test also says that semi-gel electrolyte shows the much better performance for low-rate discharge and the liquid electrolyte is good for high-rate discharge because the reaction rate of gel electrolyte is slower than liquid one for high-rate discharge performance. The test with DOD10% and DOD100% says that 5% silica electrolyte shows much better performance for life efficiency than liquid one. Because semi-gel electrolyte increase the efficiency of gas recombination at the chemical reaction of VRLA battery and it makes minimizing the reduction of electrolyte. Using the 5% silica electrolyte in order to improve the stroage efficiency and life performance for photovoltic and wind power generation, it causes improving by 4.8% for DOD100% and 20% for DOD10%.

• Proceedings of the KWS Conference
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• 2010.05a
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• pp.73-73
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• 2010

합금원소가 다량 첨가된 고합금강, 스테인리스강, Ni기 초내열합금 등은 용접시 혹은 후열처리 동안 열영향부 (HAZ: heat-affected-zone)에서 결정립계를 따라서 액화균열이 종종 발생한다. 이러한 액화균열은 급속한 가열시 HAZ의 결정립계가 국부적으로 용융되어 액상필름을 형성하고, 냉각시 수축으로 인한 인장구속응력에 의해 필름을 따라서 균열이 발생하여 생성된다. HAZ 결정립계 액화는 탄화물, 황화물, 인화물, 보론계 화합물 등이 급가열시 기지와의 반응에 의해 표피 액상을 형성하는 조성적 액화 (constitutional liquation)에 의한 액상의 결정립계 침투로 설명되거나, 결정립계 자체의 용융점을 상당량 낮추는 보론(B), 인(P), 황(S)등의 편석에 의한 국부적 입계 용융으로 주로 연관 지어 해석한다. HAZ 액화균열은 고온 입계균열 현상이므로, 결정립계의 특성에 따라 크게 영향을 받으며 결정립계 character 설계에 의해 액화균열 저항성을 개선시킬 수 있음을 유추할 수 있다. 한편, 본 연구자들은 최근 Ni기 초내열합금에 있어 입계 serration 현상을 새롭게 발견하였으며, 이론적 접근법을 통해 serration을 위한 특별한 열처리 방법을 개발하였다. 형성된 파형입계는 결정학적인 관점에서 조밀 {111} 입계면을 갖도록 분해 (dissociation)되어 낮은 계면에너지를 갖게 됨을 확인하였으며, 입계형상 변화뿐만 아니라 탄화물 특성변화까지 유도하여 크리프 수명을 기존대비 약 40% 정도 향상시킴을 확인하였다. 본 연구에서는 이러한 직선형 입계 대비 'special boundary'로 간주되는 파형입계가 도입될 경우, 보론 편석 및 HAZ 액화거동에 미치는 영향을 고찰하고자 하였다. SIMS (secondary ion mass spectrometry)를 이용하여 열처리 직후 결정립계 보론편석 정도를 비교하였다. 파형입계 시편의 경우, 일반직선형 시편에 비해 결정립계에 보론편석 저항성이 우수함을 확인할 수 있었다. 재현 HAZ 열사이클 시험을 통해 미세조직을 정량적으로 분석하였다. 파형입계 시편 및 일반직선형 시편 모두 최고온도 $1060^{\circ}C$이상부터 입계 탄화물이 기지내로 완전 용해되고 입계가 액화되기 시작하였다. 최고온도별로 입계액화비율을 정량적으로 비교한 결과, 파형입계가 직선입계 대비 훨씬 낮음을 확인할 수 있었으며, 때때로 액화된 필름이 입계를 따라 전파되지 않고 부분적으로 단락되어 있음이 관찰되었다. 액화시험 후 투과전자현미경을 이용한 EDS (energy dispersive spectrometry) 분석을 통해 결정립계 액화의 주요원인은 입계 $M_{23}C_6$의 조성적 액화반응 보다는 보론 편석 (원자 및 $M_{23}(CB)_6$)으로 인한 결정립계 국부용융이 더 유력함을 유추할 수 있었다. 따라서 상기 결과로부터 입계구조가 안정되어 계면에너지가 낮은 파형입계가 보론편석에 대한 저항성이 우수하였으며, 이러한 결과는 액화 저항성에 대응되어 영향을 미침을 알 수 있었다. 게다가 파형입계에 액상 필름이 생성되더라도 낮은 계면에너지에 의해 비롯된 상대적으로 낮은 적심성 (wettability)에 의해 필름이 쉽게 전파되지 않음을 'Smith 입계 wetting 이론'을 이용하여 해석할 수 있었다.

• Journal of the Korean GEO-environmental Society
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• v.11 no.1
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• pp.45-51
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• 2010

Cadmium (Cd) adsorption by the activated carbon containing hydroxyapatite (HAP) was investigated. Cd adsorption with different HAP mass ranged from 10% to 30%. With more HAP, more Cd was adsorbed. These results suggest that the higher HAP dose causes an increase of the ion exchange potential in HAP sorbent. Kinetics and equilibrium studies were investigated in series of batch adsorption experiments. Langmuir and Freundlich isotherm models were fit to the equilibrium data and Cd adsorption on HAP sorbent were found to follow the Freundlich isotherm model well in the initial adsorbate concentration range. The simple kinetic model, the pseudo first order kinetic model and the pseudo second order kinetic model, were used to investigate the adsorption. The adsorption reaction of Cd followed the pseudo second order kinetic model, and the adsorption pseudo second order kinetic constants ($k_2$) increased with increasing initial HAP amounts onto activated carbon. Also, intraparticle diffusion model was used to investigate the adsorption mechanism between adsorbate and adsorbent in the aqueous phase. Surface adsorption reaction and intraparticle diffusion occur simultaneously Cd adsorption mechanism from aqueous phase in this study.

• Journal of the Korean Society of Food Science and Nutrition
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• v.36 no.11
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• pp.1465-1471
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• 2007

Response surface methodology (RSM) was employed to optimize extraction conditions in order to find the maximal functional properties of fluid Cheonggukjang. Based on central composite design, a study plan was established with variations of microwave power, ethanol concentration, and extraction time. Regression analysis was applied to obtain a mathematical model. The maximum inhibitory of tyrosinase activity was found as 26.75% at the conditions of 30.56W microwave power, 2.40 g/mL of ratio of solvent to sample content and 10.00 min extraction time, respectively. The maximum superoxide dismutase (SOD)-like activity was 53.23% under the extraction conditions of 108.42 W, 4.38 g/mL and 7.84 min. Based on superimposition of three dimensional RSM with respect to extraction yield, inhibitory of tyrosinase activity and SOD-like activity obtained under the various extraction conditions, the optimum ranges of extraction conditions were found to be microwave power of $55{\sim}75$ W, ratio of solvent to sample content of $2{\sim}5$ g/mL and extraction time of $3.5{\sim}15$ min, respectively.

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.248.1-248.1
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• 2010

수송용 바이오연료로써 바이오디젤의 보급 활성화에 따른 원료인 식물성 기름의 가격 상승 및 수급 불안정성 문제를 해결하고자 그동안 활용되지 않았던 폐유지를 바이오디젤 생산 원료로 사용하여 바이오디젤 생산 단가를 낮추고 원료의 수급 안정성도 확보하려는 시도가 이루어지고 있다. 폐유지의 경우 대부분 유리지방산 함량이 높아 염기 촉매를 적용하는 방법으로는 비누의 생성으로 전환이 힘들며 산 촉매를 적용하여 유리지방산을 에스테르화하는 공정을 필요로 한다. 에스테르화 반응에서는 반응 부산물로 물이 생성되며, 생성된 물은 바이오디젤 생산 반응을 저해하고 역반응을 유도하며 촉매의 활성을 감소시킨다. 본 연구에서는 고유리지방산 함량 오일의 에스테르화 반응에서 수분의 영향을 검토하였다. 산 촉매로 액상 촉매인 황산과 고체 산 촉매인 Amberlyst-15를 사용하였다. 초기 수분 함량이 0, 1, 2, 5, 10, 20%로 증가하였을 때, 지방산 메틸 에스테르 함량이 크게 감소하였으며, 1%의 수분 함량에서도 반응이 크게 저해받는 것으로 나타났다. 따라서 고유리지방산 함량 오일의 에스테르화 반응에서 수분에 의한 저해가 중요한 변수라는 것을 알 수 있다. Amberlyst-15는 황산보다 수분의 영향에 의해 지방산 메틸 에스테르 함량이 빠르게 감소하였다. 이는 다공성의 Amberlyst-15에서 생성된 물이 반응물질들이 active site에 접근하는 것을 방해하였기 때문인 것으로 생각된다. 황산을 사용하였을 경우에는 오일 대 메탄올 몰비를 1:3에서 1:6으로 증가시킴으로써 정반응 속도가 증가하여 수분에 대한 영향이 감소하는 현상이 나타났다. 에스테르화 반응 종료 12시간 후에 바이오디젤과 메탄올 내에 수분 함량을 분석한 결과 12%의 수분이 바이오디젤 층에 존재하며 88%의 수분은 메탄올 층에 존재하였다. 반응 중에 생성된 수분을 제거하기 위해, 에스테르화 반응 30분 후에 물을 포함하는 메탄올과 촉매 층을 새 메탄올과 촉매로 교환하는 2단계 반응을 수행함으로써 지방산 메틸 에스테르 함량을 향상시킬 수 있었다. 반응 초기에는 황산이 Amberlyst-15보다 높은 활성을 보였지만, 시간이 지날수록 두 촉매 사이의 에스테르화 성능 차이는 감소하였다. 따라서 2단계 에스테르화 반응이 수분의 저해작용을 줄이는 한 가지 대안으로 제안될 수 있다. 또한 에스테르화 반응에서 물의 저해 작용을 줄이기 위해 앞으로 투과증발막의 적용 또는 물에 저해작용을 받지 않는 구조의 촉매 사용을 검토할 필요가 있다.

• Journal of the Korean Institute of Gas
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• v.21 no.3
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• pp.1-8
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• 2017

The purpose of this study is to suggest the rupture disk design(size) and application at the two phase(gas-liquid) flow by runaway reaction at batch reactor. The definition of runaway reaction is abnormally exothermic reaction by the uncontrolled cooling water or deviated operating condition. As a result, the temperature of reactor is rapidly increasing. The causes of runaway reaction are either self-heating reaction or sleeper reaction. General methods of rupture disk size or safety valve are not suitable in the runaway reaction, because of temperature and pressure increasing rapidly in the reactor and the phases of relieving fluid is 2-phase flow. This study case of the reactor incident, the depressurization system such as safety valve and vent installed, however, the system did not relieved the pressure of reactor suitably. The orifice size of the safety valve were designed too small because the size had not been considered the phenomena and character of reaction. The batch reactor design should be considered by referring to the possibility of runaway reaction proposed in this study and the size of rupture disk design method considering 2-phase flow.

• Journal of Korean Society of Environmental Engineers
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• v.29 no.1
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• pp.62-67
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• 2007

It was investigated to develop the technology for simultaneous removal of $SO_2/NO$ in flue gas using liquid homogeneous catalyst. Test was carried out using a bench scale and a pilot scale experiment. The investigation led to the following results: 1) Removal efficiency of $SO_2$ gas showed good results regardless of operating condition. Removal efficiency of NO gas, however, proportionally increased with higher packing height, lower concentration and larger injection rate of catalyst 2) The optimum design parameters for simultaneous removal of $SO_2/NO$ gas using Fe(II)-EDTA catalyst were as follow: HTU(height of transfer unit) = 0.5 m, liquid gas ratio = 20 $L/m^3$, NTU (number of transfer unit) = 3 stages, cross dimension of scrubber=0.025 $m^2$ 3) The removal efficiencies of $SO_2$ and NO were 95% and 81%, repletely. 4) The high HTU is advantageous on removal of the NO, but the excessive HTU diminishes operating efficiency. Consequently, it is important to decide the HTU of optimum.

• Applied Chemistry for Engineering
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• v.3 no.1
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• pp.172-178
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• 1992

The graft copolymerization of acrylonitrile(AN) onto chitosan film by using $F^{3+}(FeCl_3{\cdot}6H_2O)$ as a photosensitizer in an aqueous medium was carried out under ultraviolet(UV) irradiation. The grafted copolymer was identified by using IR spectroscopy and scanning electron microscope. The effects of various polymerization parameters involving monomer concentration, photosensitizer concentration, polymerization time and polymerization temperature were investigated. As monomer concentration and photosensitizer concentration were increased, the percent grafting was increased up to limiting value. And also the percent grafting was found to increase by increasing the polymerization time and temperature.

• Journal of Animal Environmental Science
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• v.11 no.1
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• pp.17-24
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• 2005

Aerobic sequencing batch reactor (SBR) was used to treat screened dairy wastewaters. The study examined the production of volatile organic compounds (VOCs) and volatile fatty acids (VFAs) in the aerobic SBR and raw manure effluent storage over 35 days. The reduction of total VFAs in the aerobic SBR was over $59\%$ removal than that of the raw manure. Acetic acid production in the aerobic SBR and the raw manure effluent storage were kept 138 and 286 mg/L. The propionic acid in the aerobic SBR was 1.9 mg/L, while the raw manure effluent storage was 68 mg/L, respectively. The concentrations of VOCs in the aerobic SBR reactor and effluent fill down remarkably than the raw manure storage. The results confirmed that the aerobic biological treatment is an essential requirement for minimizing odor problems.