• Applied Chemistry for Engineering
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• v.20 no.6
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• pp.675-680
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• 2009

This article describes NO emission characteristics in SM coal combustion. Combustion experiments was performed in the method of increasing temperature after feeding coal and feeding coal after increasing temperature. NOx emission is in inverse proportion to combustion temperature at the fuel rich condition and it was caused by conversion fuel N to $N_{2}$ at the strong reduction condition. In addition, feeding gas flow rate increased as total fuel NOx increase by conversion of fuel N to NO at the oxidation condition. It could be separated in total fuel-N, volatile-N, char-N to NO according to analysis of total fuel NO emission from char combustion at each temperature. In the result, almost total NOx emission was caused by volatile-N in SM-coal.

• Korean Journal of Agricultural and Forest Meteorology
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• v.4 no.1
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• pp.58-63
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• 2002

Since the rapid urbanization period coincides with the start of global warming, climate data might be contaminated with urbanization effect in Korea. Monthly normals of daily minimum, maximum, and mean temperature of 14 stations were calculated for 1951-1980 and 1971-2000 periods. Differences in two temperature normals were regressed to the natural logarithms of population increase at corresponding 14 cities from 1966 to 1990. The regression models were used to remove potential effects of urbanization from the apparent warming, and to determine the net contribution of global warming to the temperature change in Korea during the recent half century. According to the model calculation, there was little evidence of global warming in the warm season (May through November), while urbanization effect was common in all season except April. Up to 0.5$^{\circ}C$ warming of nighttime temperature was found to be induced by urbanization. Cool season temperature was increased by up to 0.6$^{\circ}C$ due mainly to the global warming of daytime temperature.

• Korean Chemical Engineering Research
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• v.48 no.6
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• pp.684-689
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• 2010

We synthesized a variety of SAPO catalysts with various structure directing agents by the hydrothermal method and applied them to the D-xylose dehydration. Single or mixtures of organic amines, viz. tetraethylammonium hydroxide(TEAOH), dipropylamine(DPA), diethylamine(DEA), morpholine and diethanolamine(DEtA) were used as structure directing agents. The $N_2$-isotherm, $NH_3$-temperature programmed desorption(TPD) and temperature programmed oxidation(TPO) were conducted to characterize SAPO catalysts. Among tested SAPO catalysts, the SAPO-34 synthesized with morpholine showed the highest furfural yield. The external surface area as well as the surface concentration of acid sites appeared to affect the catalytic activity for the dehydration of xylose into furfural.

• Polymer(Korea)
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• v.37 no.2
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• pp.240-248
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• 2013

The curing behaviors of diglycidyl ether of bisphenol A (DGEBA) with mercaptan hardener were studied by the comparison with amine-adduct type hardener. Curing behaviors were evaluated by DSC at dynamic and isothermal conditions. In the DSC, the dynamic experiments were based on the method of Kissinger's equation, and the isothermal experiments were fitted to the Kamal's kinetic model. Activation energy of epoxy/amine-adduct type hardener was ca. 40 kcal/mol. As the functional group of mercaptan hardener, -SH increased, on epoxy/mercaptan hardeners, the activation energies decreased from 28 to 19 kcal/mol. Epoxy/amine-adduct type hardener was initiated at $90^{\circ}C$ or higher. However, epoxy/mercaptan hardeners reduced the initiation temperatures below $80^{\circ}C$ and shortened the durations of curing reaction within 10 min. We found out that the reaction kinetics of epoxy with mercaptan hardener followed the autocatalytic reaction models, and the maximum reaction rates were shown at the conversions of 20~40%.

• Elastomers and Composites
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• v.38 no.4
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• pp.326-333
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• 2003

Even though many studies have been reported about rubber vulcanization, it is still remained difficult to find a quantitative relationship between the final states of vulcanized rubber and initial formulation or processing conditions. Dynamic differential scanning calorimetry (DSC) method is known as a comparatively easy method to research for the rubber vulcanization in both experimental and analysis. In the present research, a study on the vulcanization reaction of NR/CB composites modified by isoprene(IR) and chloroprene(CR) rubbers is carried out using dynamic DSC method. Thermograms with several different heating rates were obtained and analyzed using the Kissinger method. Analysis showed that the vulcanization reaction was progressed through the first order reaction mechanism. In addition, the reaction temperature was severely influenced by the kinds or rubber modifiers, in this case, more influenced by CR than by IR. Those effects were clearly verified in the values of activation energy. Kinds of carbon blacks, however, could hardly influence on the reaction mechanism.

• Proceedings of the Korean Vacuum Society Conference
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• 2011.08a
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• pp.324-325
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• 2011

최근에 고효율의 적색 형광체를 합성하여 형광 램프, 음극선관, X-선 검출기, 전계 발광 디스플레이에 응용하기 위하여 다양한 모체 결정과 활성체를 도핑하는 연구가 활발히 진행되고 있다. 본 연구에서는 $GdNbO_4$ 모체 결정에 $Eu^{3+}$ 이온 활성체를 주입하여 합성함으로써 새로운 적색 형광체의 발광 세기와 입자의 형상을 최적화 시키고자 한다. 형광체 분말 시료의 제조는 Eu의 함량을 0, 0.05, 0.10, 0.15, 0.20 mol로 변화시키면서 고상 반응법을 이용하여 합성하였다. 초기 물질 Gd2O3 (99.99%), $Nb_2O_5$ (99.99%), $Eu_2O_3$ (99.9%)를 화학 적량으로 측량하고 에탄올과 ZrO2 볼과 함께 플라스틱 병에 넣어 400 rpm의 속도로 24시간 볼밀 작업을 수행한 후에, 혼합된 분말의 볼을 걸러내고 60$^{\circ}C$에서 20시간 동안 건조하였다. 건조된 시료를 막자 사발에 넣고 잘게 갈아서 체로 걸러낸 다음에 세라믹 도가니에 넣고 전기로에서 분당 5$^{\circ}C$씩 승온하여 500$^{\circ}C$에서 10시간 동안 1차 하소한 후에, 계속 온도를 승온시켜 1,200$^{\circ}C$에서 3시간 동안 소결하여 합성하였다. XRD 회절 패턴의 경우에, $Eu^{3+}$의 함량에 관계없이 모든 세라믹은 JCPDS (22-1104)에 제시된 회절상과 일치하는 사방정계의 결정 구조를 가짐을 확인할 수 있었다. 주 피크는 28.4$^{\circ}$에서 최대값을 갖는 (121)면에서 발생하는 회절 신호이었다(Fig. 1). 적색 형광체 분말의 광학 및 표면 특성은 PL, PLE와 SEM으로 조사되었으며, 세라믹 분말의 형광 특성과 결정 구조, 표면 형상에 대한 자세한 논의가 제시될 것이다.

• Journal of the Korean Magnetics Society
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• v.11 no.1
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• pp.26-31
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• 2001

The effect of MoO$_3$ addition on the permeability of Mn-Zn ferrites was studied. 600 ppm, 800 ppm and 1,000 ppm of MoO$_3$ were added to the main composition after calcination. Ferrite cores were sintered at 135$0^{\circ}C$ for 3hrs, followed by cooling according to the equilibrium oxygen concentration. The initial permeability was about 8,000 with heating rate 5$^{\circ}C$/min for 3hrs without MoO$_3$ addition. When 600 ppm and 800 ppm of MoO$_3$ were added, the initial permeabilities, 13,200 and 13,550 were obtained, respectively. However, the sample with 1,000 ppm MoO$_3$ showed lower permeabilities because of abnormal grain growth. At the heating rate 1$0^{\circ}C$/min, the ferrite cores with 1,000 ppm MoO$_3$ demonstrated the highest initial permeability greater than 15,000, without exaggerated grain growth.

• Journal of the Korea Convergence Society
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• v.8 no.3
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• pp.169-176
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• 2017

Casting process includes wax pattern, investment, dewaxing, curing, casting, etc., and each single process is important to achieve a good result. Since 2000, 3D printers have been developed and widely used; as more prefer UV Curavle resin method over wax method, resultant casting defects have become worse. To resolve such problem, preceding research revealed casting defects of existing wax method. In particular, defects of UV Curavle resin method showed difference in investment, dewaxing, deresinating and curing compared to the existing one. Accordingly, results were presented through casting tests; especially, a temperature rising curve only for UV Curavle resin was shown rather than one for the existing method. Lastly, this research classified those not available with direct casting and suggested mold manufacturing. This research is expected to be useful for 3D printer users or those who would conduct direct casting with UV Curavle resin.

• Resources Recycling
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• v.8 no.4
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• pp.3-10
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• 1999

An experimental study for manufacturing lightweight aggregates from sewage sludge ash of sewage treatment facilities was carned out in senses of sludge disposal and utilization. In case of SA alone, aggregates with S.G. 1.67 was obtained at sintering temperature of $1250^{\circ}C$, and heating rate affects little to volume expansion rate and volume expansion rate was decreased more or less by heating time. In case of adding 10 wt% of RFCC to SA, lightweight aggregates with S.G. 1.07 was obtained and volume expansion rate was increased by heating time. The optimum adding amounts of RFCC to manufacture lightweight aggregates was 10wt% and the condition that shows maximum volume expansion rate was $20^{\circ}C/min$ of heating rate, $1250^{\circ}C$ of sintering temperature and 50 mmutes of heating time. According to adding amounts of RFCC, Compressive strength of sample results in 30 wt% RFCC>SA>20 wt% RFCC>10 wt% RFCC.

• Solar Energy
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• v.15 no.1
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• pp.29-38
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• 1995

This paper concerns the study of a two-stage binary absorption cycle employing the refrigerant/absorbent combinations of $LiBr/H_2O$ and $NH_3/H_2O$. This cycle consists of coupling two single-effect absorption cycles so that the first stage absorber and condenser produces heating water to evaporate refrigerant in the evaporator of the second stage. The effect of operating variables such as evaporator temperature, condenser and absorber temperature, and generator temperature on the coefficient of performance and temperature lift have been studied for two-stage binary absorption heat pump systems. It is found that this cycle has a large temperature lift at $105^{\circ}C$ of optimum generator temperature to obtain $50^{\circ}C$ of condenser temperature.