• 한국토양비료학회지
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• 제27권1호
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• pp.10-14
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• 1994

지효성 K비료는 KOH, KCl 등 속효성 K원료와 Fly ash중 난용성 K를 이용하였고 소성시 보조제로서 부연탄가루, $Mg(OH)_2$, $K_2CO_3$와 Borax를 혼합하여 제조하였다. 목표 K함량에 맞게 원료와 보조제 혼합비율이 결정되었으며 무연탄가루와 $Mg(OH)_2$의 적정 배합비율은 각각 12%, 3%이었으며 소성온도는 $850^{\circ}C$, 소성시간은 30분이 적정선으로 판명되었다. 시제품은 소성온도가 낮고 소성시간이 짧은 경우 시제품의 특성에 부적합하였다. 제조된 시제품의 K성분은 지효화되어 목표치에 부합되었다.

• 한국응용과학기술학회지
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• 제35권3호
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• pp.757-767
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• 2018

고온에서 진행되는 프로판 탈수소 반응에서 촉매의 불활성화의 주된 원인은 코크 침적, 소결현상이 있다. 이러한 불활성화를 줄이는 촉매를 연구하기 위해, 본 연구에서는 열적 안정성이 높은 $MgAl_2O_4$ 를 담체로 적용하여 프로판 탈수소 반응용 촉매로의 활용성을 확인하고자 하였다. Alcohthermal method로 $MgAl_2O_4$를 소성온도 800, 900, $1000^{\circ}C$로 달리하여 제조하였고, Pt와 Sn을 공동함침법으로 담지하여$Pt-Sn/MgAl_2O_4$촉매를 제조하였다. 열적안정성의 확인을 위해 반응온도를 고온의 650, $600^{\circ}C$에서 진행하였다. 반응실험 결과 반응온도에 상관없이 담체의 소성온도가 $800^{\circ}C$인 담체적용 촉매일 때 프로판 탈수소반응 실험의 전환율과 수율이 담체소성온도가 900, $1000^{\circ}C$인 담체적용 촉매보다 높은 것을 확인하였고, 반응온도가 고온인 $650^{\circ}C$일 때는 $Pt-Sn/{\theta}-Al_2O_3$보다도 더 높은 수율을 가지는 것을 볼 수 있었다. 특성분석으로는 TGA, BET, XRD, CO-화학흡착, SEM-EDS 분석을 실시하였다. $MgAl_2O_4-800^{\circ}C$가 좋은 수율과 Pt분산도 및 적은 불활성화 정도의 관계를 서로 연관 지어 확인하였다.

• 환경위생공학
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• 제15권1호
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• pp.62-68
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• 2000

This study was investigated to the recovery of alumina from the first calcined waste pottery using alkaline sintering. This study was based on calcination result of a commercial ${\alpha}-Al2_O_3$ with NaOH powder. $NaAlO_2$ was formed by calcination of ${\alpha}-Al_2O_3$ with NaOH and conversion of $NaAlO_2$ from ${\alpha}-Al_2O_3$ was 91.4% at calcination condition ; weight ritio of $NaOH/{\alpha}-Al2_O_3$ 1.5, $800^{\circ}C$, and 90min. The first calcined waste porrery from the manufacturing Procedure of H Ltd. was grinded to 170/270mesh by a ball mill and calcined over $500^{\circ}C$ with NaOH powder. The calcined sample was dissolved in $25^{\circ}C$ water and sodiumaluminosilicate solid was formed. After filtration, the contained aluminum was leached out by dissolving sodiumaluminosilicate solid in 1N HCl. We estimated the efficiency of Al extraction from waste pottery by ICP analysis and NaOH was added to the filtrate and then aluminum compound was precipitated with $Al(OH)_3$ and recovered. The investigation was carried out with the variables ; the calcination temperature($500-900^{\circ}C$), the calcination time(30~90min), and the weight ratio of NaOH/waste pottery(0.5~1.5). The treatment efficiency of the waste pottery and the recovery of Al as 97.9%, 91.9% were obtained under the optimum conditions as followed ; the weight ratio of NaOH/waste pottery was 1.5 and the calcination conditions were $900^{\circ}C$ and 60min.

• 한국분말재료학회지
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• 제16권3호
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• pp.191-195
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• 2009

The calcination and hydrogen-reduction behavior of Fe- and Ni-nitrate have been investigated. $Fe_2O_3$/NiO composite powders were prepared by chemical solution mixing of Fe- and Ni-nitrate and calcination at $350^{\circ}C$ for 2 h. The calcined powders were hydrogen-reduced at $350^{\circ}C$ for 30 min. The calcination and hydrogen-reduction behavior of Fe- and Ni-nitrate were analyzed by TG in air and hydrogen atmosphere, respectively. TG and XRD analysis for hydrogen-reduced powders revealed that the $Fe_2O_3$/NiO phase transformed to $FeNi_3$ phase at the temperature of $350^{\circ}$. The activation energy for the hydrogen reduction, evaluated by Kissinger method, was measured as 83.0 kJ/mol.

• 환경위생공학
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• 제18권3호통권49호
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• pp.48-58
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• 2003

To obtain the preliminary design data for combustion of paper sludges, decomposition characteristics and combustion kinetics of paper sludges reactor have been determined in a TGA reactor. Also, the combustion characteristics of paper sludges have been determined in a fluidized bed reactor. The data obtained from the TGA reactor indicate that dewatering of paper sludge is terminated at temperature below 130${\circ}$C. With heating rate of 20${\circ}$C/min, combustion is terminated at temperature below 340${\circ}$C .The combustion rate is found to be first order with respect to temperature and oxygen concentration. Activation energies for paper wastes are found to be 570, 700, 2600, 4600 Kcal/mole, respectively. The calcination conversions were investigated with the operating temperature and residence time. In this investigation, it was found that calcination conversion was affected by the operating temperature and residence time. The optimum conditions of operating temperature and mean residence time were 850${\circ}$C and 6 minutes of respectively.

• 한국세라믹학회지
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• 제51권5호
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• pp.413-417
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• 2014

The effect of calcination treatment of raw powders prior to high temperature synthesis of Ca-${\alpha}$-SiAlON:$Eu^{2+}$ phosphor was investigated. Based on data acquired from thermogravimetric analysis, calcination temperatures were set at 600, 750, and $900^{\circ}C$. Compared to the photoluminescence (PL) intensity of direct synthesis without calcination, a similar intensity was found for the $600^{\circ}C$ treatment, a 19% increased PL intensity was found for the $750^{\circ}C$ treatment, and a 23% decreased PL intensity was found for the $900^{\circ}C$ treatment. Observation of the particle morphology of the synthesized phosphors revealed that the material transport promoted through the agglomerates formed by the $750^{\circ}C$ treatment led to enhanced PL intensity. On the other hand, the oxidation of the starting AlN particles during the $900^{\circ}C$ treatment resulted in decreased photoluminescence.

• 대한안전경영과학회지
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• 제21권1호
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• pp.17-23
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• 2019

The diesel engine generate many pollutants such as PM(Particulate matter) and NOx(Nitrogen oxide). So the SCR(Selective catalytic reduction) must be required to meet the emission standard. The SCR catalyst market is growing rapidly, and the automobile markets using alternative energy sources are growing rapidly. This study deals with optimization of the calcination process the manufacturing process of SCR catalyst to be competitive. The calcination process is a bottleneck and it is required to optimize productivity and accept to be safety, But we cannot trade off anything in terms of safety. We applied DOE(Design of experiments) among many research methods performed in various fields. In order to achieve quality and productivity optimization. The dependent variables in the DOE were selected as NO Conversion(%). The independent variables were selected as the calcination temperature, soaking time and fan speed RPM. the CCD(Central composite designs) constructs response surface using the data onto experience and finds optimum levels within the fitted response surfaces. Our tests are our stability guarantee and efficient together with operation.

• 한국재료학회지
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• 제22권1호
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• pp.54-60
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• 2012

The particle size of MgO was examined as a function of the Na content in $Mg(OH)_2$ powders and the calcination temperature. $Mg(OH)_2$ suspension was obtained by dropwise precipitation of $Mg(NO_3)_2{\cdot}6H_2O$ and NaOH solutions. The suspension was diluted by varying the dilution volume ratio of distilled water to $Mg(OH)_2$ suspension to change the Na salt concentration in the suspension. $Mg(OH)_2$ slurry was filtered and dried at $60^{\circ}C$ under vacuum, and then its $Mg(OH)_2$ powder was calcined to produce MgO with different amount of Na content at $500\sim900^{\circ}C$ under air. Investigation of the physical and chemical properties of the various MgO powders with dilution ratio and calcination temperature variation was done by X-ray diffraction, transmission electron microscopy, BET specific surface area and thermal gravimetric analysis. It was observed that MgO particle size could depend on the condition of calcination temperature and dilution ratio of the $Mg(OH)_2$ suspension. The particle size of the MgO depends on the Na content remaining in the $Mg(OH)_2$ powder, which powder was prepared by changing the dilution ratio of the $Mg(OH)_2$ suspension. This change increased as the calcination temperature increased and decreased as the dilution ratio increased. The growth of MgO particle size according to the increase of temperature was more effective when there was a relatively high content of Na. The increase of Na content lowered the temperature at which decomposition of $Mg(OH)_2$ to MgO took place, thereby promoting the crystal growth of MgO.

• 공업화학
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• 제10권8호
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• pp.1109-1113
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• 1999

함침법에 의하여 제조된 $Pt/MoO_3$와 $Pt/MoO_3/SiO_2$ 및 $Pt^{\circ}$와 $MoO_3$를 기계적으로 혼합한 촉매를 사용한 $50^{\circ}C$ 등온 환원 실험에서 소성 온도가 증가할수록, $H_2$ spillover에 의하여 Pt로부터 $MoO_3$로 이동하여 저장되는 $H_2$가 증가하는 것을 측정하였다. 연속적으로 실행한 CO chemisorption에 의하여 $H_2$ spillover에 참가하는 $H_2$에 노출된 Pt 표면적이 감소하는 것을 알 수 있었다. 또한, TEM 결과로부터 $400^{\circ}C$에서 소성 후 Pt결정 표면에 $MoO_x$ overlayer가 형성되는 것을 관찰하였다. 그러므로, 표면 형상 변화에 따른 Pt과 $MoO_3$간의 활성접촉점 증가가 $H_2$ spillover에 의한 $MoO_3$로의 $H_2$ 이동을 증가시키는 원인 중의 하나인 것으로 판명된다.

• 한국자기학회지
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• 제19권6호
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• pp.216-221
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• 2009

Y-type 바리움 페라이트 $Ba_2Co_2Fe_{12}O_{22}$를 고상반응법으로 제조하고 금속이온몰비($Fe^{3+}:\;Ba^{2+}:\;Co^{2+}$)와 열처리 온도가 자기적 성 질과 미세구조에 미치는 영향에 대하여 조사하였다. 상분석과 미세구조는 각각 XRD(X-ray diffractometer)와 FESEM(field effect scanning electron microscope)을 이용하여 조사하였으며 분말의 자기적 성질은 VSM(vibrating sample magnetometer)을 이용하여 조사하였다. 금속이온몰비($Fe^{3+}:\;Ba^{2+}:\;Co^{2+}$)가 6 : 1 : 1인 조성의 분말을 $1050\;{^{\circ}C}$에서 열처리하였을 때 단일 상이 합성되었으며 8 : 1 : 1인 조성의 분말을 $1200\;{^{\circ}C}$에서 열처리하였을 때 가장 높은 포화자화값(39.1 emu/g)을 나타내었다.