• Journal of the Korea Academia-Industrial cooperation Society
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• v.5 no.1
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• pp.34-37
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• 2004

Effect of $H_2$ spillover rate as functon of calcination temperature on reaction kinetics was evaluated. Reaction kinetics including yield, conversion and selectivity of 1-butene isomerization over $Pt/HxMoO_3/SiO_2$ were measured as reaction temperature was increased. While conversion of 1-butane was decreased, yield of iso-butene was increased. Two kinds of reaction mechanism were proposed from the change of selectivity as function of temperature.

• Proceedings of the Korean Society of Propulsion Engineers Conference
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• 2017.05a
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• pp.1036-1037
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• 2017

This study investigated the aging reactions of three kinds of igniters(BKNO3, THPP, ZPP). The life-time of igniter depends on oxygen and moisture in the air. For example, Magnesium contained in the $BKNO_3$ reacts with oxygen and water to form oxide and hydrate. This reaction has an adverse effect on ignition reaction and could be information to analyze aging. Thermodynamic calculation could interpret the aging reaction by calculating flame temperature applying several variables(initial temperature, composition, etc.). If combustion is not completed because of aging igniters, flame temperature will be formed at a low range. The result of this research is expected to support the analysis of igniters aging reactions.

• 한국신재생에너지학회:학술대회논문집
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• 2010.11a
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• pp.129.1-129.1
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• 2010

석탄가스화로부터 얻어진 합성가스는 CO, $H_2$가 주성분으로, 그 자체를 연료로 사용하여 발전을 하거나 또는 적절한 정제, 분리 및 합성을 통해 다양한 원료물질을 생산할 수 있다. 이러한 석탄의 청정 사용 기술은 최근의 에너지 분야에서 많은 관심을 불러일으키고 있는 고유가 현상 및 석유자원 고갈에 대비할 수 있는 현실적인 방법의 하나로 여겨지고 있다. 석유를 대체할 에너지원으로서 석탄을 이용하는 다양한 응용 방법 중의 하나로 가스화 반응을 통해 발생하는 합성가스를 이용한 SNG 제조 공정을 들 수 있는데, 이는 석탄 등의 고체 시료를 이용하여 메탄이 주성분인 연료가스를 생산하는 것이다. SNG(Synthesis Natural Gas 또는Substitute Natural Gas)는 합성천연가스 또는 대체천연가스로 불리어지는데 주로 석탄의 가스화를 통해 얻어진 합성가스(syngas 또는 synthesis gas)인 CO, $H_2$를 촉매에 의한 합성반응을 통해 얻을 수 있다. SNG 합성 반응(메탄화 반응)은 보통 수성가스 전환 공정과 가스 정제 공정을 거친 합성가스를 $CH_4$로 전환하는 것으로 석탄을 이용한 SNG 제조 공정에서 가장 핵심 공정인 메탄화 반응은 높은 발열반응으로 주로 니켈 촉매를 사용하며 $250{\sim}400^{\circ}C$에서 반응이 이루어진다. SNG 합성 반응은 공급되는 합성가스의 조성($H_2$/CO 비), 공급되는 합성가스의 유량과 반응기에 충진된 촉매의 부피와의 관계를 나타낸 공간속도, 반응온도 등의 조건에 따라 반응 특성이 달라질 수 있다. 가스화 반응을 통해 생성되는 합성가스를 이용한 SNG 합성반응(메탄화 반응)의 특성을 파악하기 위하여 Lab-scale 규모의 고정층 반응기를 이용하여 Ni 함량이 다른 2종류의 촉매를 대상으로 반응온도 및 압력에 따른 CO 전환율, $CH_4$ 선택도, $CH_4$ 생산성 변화를 파악하였다. 실험 결과 반응기의 온도가 350도 이상의 조건에서 CO 전환율은 99.8%이상, $CH_4$ 선택도는 90.7%이상으로 나타났으며, 공간속도가 2,000 1/h 이상의 조건에서는 $CH_4$ 생산성이 500 ml/g-cat, h을 만족하였다.

• Journal of the Korean Wood Science and Technology
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• v.43 no.6
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• pp.838-850
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• 2015

In this study, dilute acid pretreatment was operated using small-diameter Quercus mongolica for evaluating the yield change of furfural and levulinic acid depending on pretreatment factors. The dilute acid pretreatment was conducted depending on reaction temperature ($140-180^{\circ}C$), reaction time (10-30 min), and sulfuric acid concentration (0-2%, w/w). Then, glucose, XMG (xylose + mannose + galactose), furfural, and levulinic acid contents in the liquid hydrolyzate were measured and analyzed after pretreatment. Glucose content increased to 16.02% as reaction temperature, reaction time, and sulfuric acid concentration increased, but it decreased at the sulfuric acid concentration of 2% (reaction temperature: > $170^{\circ}C$, reaction time: > 20 min). On the other hand, reaction temperature had a strong influenced on XMG content, and XMG content decreased to 1.63% through increasing of reaction temperature and sulfuric acid concentration, but XMG content was less affected by changes of reaction time. Furfural content increased with the increase of reaction temperature, reaction time, and sulfuric acid concentration, and maximum furfural content was 7.61% (reaction temperature: $180^{\circ}C$, reaction time: 20 min, sulfuric acid concentration: 1%) based on a weight of raw material, while furfural content was dropped in more severe condition than in maximum furfural content condition. Levulinic acid content also increased with higher reaction temperature, reaction time, and sulfuric acid concentration. Especially, the sharp increase of levulinic acid content was observed above $170^{\circ}C$, and maximum levulinic acid content was 10.98% (reaction temperature: $180^{\circ}C$, reaction time: 30 min, sulfuric acid concentration: 2%). However, less than 1% of furfural and levulinic acid content was obtained in non-acidic catalyst condition that in whole conditions of reaction temperature and reaction time.

• Proceedings of the KAIS Fall Conference
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• 2012.05a
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• pp.356-359
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• 2012

SNCR 기술은 SCR에 비해 탈질 효율은 떨어지지만 촉매없이 고온 배출가스에 NH3 또는 요소수를 직접 분사하여 질소와 물로 환원시키는 방법이므로 초기 투자비 및 운영비가 적어 최근 국내 대다수의 소각장, 산업용 보일러 등에 널리 적용되고 있다. 단, SNCR 기술은 급격한 온도 강하나 접근의 불용이성, 불균일한 혼합, 액적의 증발시간 지연, 불균일한 운전 조건 등의 영향을 크게 받으며, 특히 반응 온도가 가장 중요한 변수로서 최적 반응 온도 영역대가 약 800~$1,000^{\circ}C$라는 점에서 이상적인 반응 온도 조건을 찾아서 환원제를 분무하는 것이 매우 중요하다. 이에 본 연구에서는 열유동 전산해석을 통해 스토커식 소각로의 폐기물 성상별 화염 온도 분포를 예측하고 적정 반응 온도 영역을 확인하여 요소수 주입 고도를 선정, 폐기물 성상별 분무 조건을 확립하고자 수치 해석적 연구를 수행하였다. 폐기물 성상(고질/중질/저질 폐기물)별로 화염 온도를 예측한 결과, 최적 반응 온도 영역대가 약 800~$1,000^{\circ}C$, 폐기물 성상의 심한 변화 때문에 소각로의 효율적인 연소 조건 제어에 어려움 등을 고려하여 약 700~$1,000^{\circ}C$ 온도 영역대를 환원제 분무 온도로 선정하였다. 폐기물별로 발열량에 따른 화염 온도가 모두 다르기 때문에 환원제 분무 위치를 3지점으로 선정하여 각 지점별로 분무 운전 조건을 확립하였다.

• KSBB Journal
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• v.17 no.6
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• pp.543-548
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• 2002

The enantioselective esterification of racemic ibuprofen catalyzed by a Candida rugosa lipase was studied according to reaction conditions such as a lipase concentration, reaction temperature, alcohol chain length and alcohol concentration. The S-(+)-ibuprofen alkyl esters prepared were converted to S-(+)-ibuprofen by hydrolysis with sulfuric acid as a catalyst. High conversions in the esterifications were obtained at 60$^{\circ}C$ and an equimolar ratio of octanol to ibuprofen. The initial reaction rate of the esterification decreased with increasing octanol concentration. Conversion and initial reaction rate increased with increasing alcohol chain length. Values of enantiomeric excess(ee) according to esterification reaction conditions did not change below 60$^{\circ}C$. On the other hand, values of conversion and ee for the chemical hydrolysis of S-(+)-ibuprofen alkyl esters were independent of alcohol alkyl chain length. Optical resolution of racemic ibuprofen was achieved by lipase catalyzed esterification and chemical hydrolysis. The separation method provided a high yield and enantioselectivity for the production of S-(+)-ibuprofen from racemic ibuprofen.

• Clean Technology
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• v.3 no.1
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• pp.106-113
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• 1997

The objectives of this study were to investigate the characteristics of limestone calcination and sulfation in a fluidized bed reactor with bed temperature and air velocity. The experimental results were presented as follows ; First, the bed temperature had a great influence on the calcination and the sulphur retention of limestone and paper sludge. In paper sludge, the optimum conditions in calcination and desulfurization temperature was at $800^{\circ}C$ and in natural limestone, that was at $850^{\circ}C$ or $900^{\circ}C$. Second, as air velocity increased, the specific surface area of particles decreased. But the difference of surface area according to air velocity was not too large. The specific surface area of paper sludge was larger than that of natural limestone. Third, as air velocity increased, the absorbed amount of sulfur dioxide decreased. And the absorbed amount of sulfur dioxide by paper sludge was larger than that of by natural limestone. Therefore, we knew that paper sludge was excellent absorbent and bed temperature had a great important variable on the calcination and sulphur retention in a fluidized bed.

• Journal of the Korean Society of Clothing and Textiles
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• v.15 no.4 s.40
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• pp.351-365
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• 1991

본 연구에서는, 수면환경의 열적 쾌적도의 측정방법으로서 생리적 반응 뿐만 아닌 국소자극의 반응에 대한 평가법 (Allesthesial Response)에 의 한 가능성을 제시 하고자 하였다. 피험자는 19세에서 22세의 건강한 독일 여자 대학생 5명이며, 실험은 12월과 1월 독일의 KASSEL에 있는 Marburg대학 연구소의 인공기후실에서 이루어졌다. 사용의복은 면 $100\%$의 잠옷이며, 침구는 메트리스와 Wool 담요(두께 180 mm)를 사용하였다. 국소자극 반응의 온도는 $20.0^{\circ}C,\;22.5^{\circ}C,\;25.0^{\circ}C,\;27.5^{\circ}C,\;30.0^{\circ}C,\;32.5^{\circ}C$의 set가 사용되었으며, 온도자극은 Pottier Thermode type PKE 36 HO2-1 (독일, Peltroil사)로서, 온도의 도달정 밀도는 60내지 90초 동안에 각 자극온도의 변화조절이 가능하였다. 수면환경 온도는 $15^{\circ}C,\;18^{\circ}C,\;21^{\circ}C,\;24^{\circ}C,\;27^{\circ}C$의 다섯 환경으로 조절하였으며, 습도는 RH $45\%$였다. 수면환경 $18^{\circ}C$에서 $24^{\circ}C$까지에서는, 수면전, 수면후 모두, 피험자는 약간의 Hypothermia의 경향을 보였지만 Neutral Situation과 큰 차이는 나타나지 않았다. 수면전과 수면후의 체온조절 반응의 차이가 Allesthesial Response와 국소의 쾌적한 온도 선택의 두 실험결과 모두에서 현저히 나타났다. 생리적 반응의 결과에서도 $18^{\circ}C$에서 $21^{\circ}C$까지의 수면환경이 가장 쾌적하게 나타났다. 또한, 실험결과에서 행동적 온도 조절 반응이 생리적 반응에 앞서 보다 민감하게 이루어짐을 볼 수 있었다

• The Korean Journal of Food And Nutrition
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• v.17 no.3
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• pp.313-321
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• 2004

Separation-concentration of sulfur containing heterocyclic compounds(SCHC) from many reaction meat flavors manufactured with Maillard reaction was carried out. Profile of SCHC was identified and analyzed by GC and GC-MSD. The results were as follows. 1. Profile of SCHC could be identified 7 kinds thiazole and 11 kinds thiophene, the major produced compounds were thiophene, thiazolidine, 4-methyl-5-thiazole ethanol. 2. In the case of SCHC, relationship between changes of reaction conditions and the kind of produced components were as same, but produced amounts appeared the difference. Producing amount of complexed SCHC and caramellike note as well as oxygen containing heterocyclic compounds were high level more than high reaction temperature and long time reaction period. 3. Producing ratio of comparative simple structural SCHC were the highest level at reaction conditions of moisture content 50%, reaction temperature 100$^{\circ}C$ and reaction time 2 hours. Reaction conditions for the revelation of reaction meat flavor were below 110$^{\circ}C$ and less than 2 hours. 4. Relationship between moisture content and reaction temperature as well as reaction time had very relative relation. From the change of moisture content and reaction conditions could be obtained the simultaneously profile. Signal presentation for production of reaction meat flavor could be from extraction-separation-concentration of SCHC through simplification of raw-materials in the flavor and seasoning food industry.

• Korean Chemical Engineering Research
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• v.47 no.3
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• pp.287-291
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• 2009

The heterogeneous decomposition of ammonia on a quartz surface in an inverted, stagnation-point flow reactor was investigated using a measurement reactor and a numerical model of the reactor. In the experiments, 8 mole% of ammonia in nitrogen was used and the temperature of an electric heater was set in the range $300{\sim}900^{\circ}C$ to heat the quartz surface where the decomposition took place. Gas temperatures and ammonia concentrations in the reactor obtained using in situ Raman spectroscopy were analyzed with the numerical model and it was revealed that, depending on the heater temperature, the temperature of the quartz surface was estimated to be in the range $235{\sim}619^{\circ}C$ and the activation energy of the decomposition on the surface was in the range 10.9~15.8 kcal/mol.