• Korean Journal of Materials Research
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• v.7 no.4
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• pp.295-302
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• 1997

금속분말 Fe와 Si에 KNO$_{3}$(Fe+Si)무게비=0.2로 점화촉매 KNO$_{3}$를 혼합하고 50MPa로 성형한 후 점화시키는 비기체연소합성(SHS; Self propagating High temperature Synthesis)법으로 출발 분말을 얻었다. 점화분위기를 공기 및 Ar으로 한 경우 XRD결과에서 특별한 차이가 없었고 두 경우 모두 SiO$_{2}$피크가 검출되었다. 합성된 분말을 성형한 후 119$0^{\circ}C$환원분위기에서 소결하고 포석온도이하에서 열처리하여 반도성 FeSi$_{2}$가 주상인 Fe-Si계 열전재료를 제조하였다. Fe/Si무게비=46/54,44/56 및 42/58시편의 제벡계수는 Si함량이 증가할수록 증가하였다. 점화후의 세척처리를 2단계로 하는 경우 제벡계수의 부호가 변화하여 p-type에서 n-type으로 변화하며 소결밀도가 크게 상승하였다. 조성에 관계없이 공통적으로 발견되는 SiO$_{2}$는 점화시의 분위기보다는 점화촉매에 포함된 K성분이 소결 및 열처리시 산화제로 작용하여 형성되는 것이 확인되었다.

• Transactions of the Korean Society of Automotive Engineers
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• v.7 no.9
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• pp.10-19
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• 1999

In this study , a simple method has been developed to detect the required spark voltage by using the primary spark voltage instead of the secondary spark voltage. Through engine motoring experiments, this method testified to be quite satisfactory. Though the required spark voltage is affected by many in-cylinder conditions, temperature is one of the most important factors. The temperature increases significantly by combustion and the required spark voltage also changes by the temperature during the expansion stroke. On the basis of this fact, misfire can be monitored by comparing the required spark voltage between compression stroke and expansion stroke. So, in this study, two step ignition method is introduced to monitor combustion at expansion stroke. The test result shows that this method can be used to detect complex misfire pattern.

• Proceedings of the Korea Society for Energy Engineering kosee Conference
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• 2010.04a
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• pp.59-63
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• 2010

Seven different size of orifice were applied in a constant volume combustion chamber for evaluating the effects of torch-ignition on combustion. The initial flame development and flame propagation were analyzed by the mass fraction burn and combustion enhancement rate. The combustion pressures were measured to calculate the mass fraction burn and the combustion enhancement rates. In addition, the flame propagations were visualized by the shadowgraph method for the qualitative comparison. The result showed that the combustion pressure and mass burned fraction were increased when using the torch-ignition device. The combustion enhancement rates of torch-ignition cases were improved in comparison with conventional spark ignition. Finally, the visualization results showed that the torch-ignition induced faster burn than conventional spark ignition due to the earlier transition to turbulent flame and larger flame surface, during the initial stage.

• Fire Science and Engineering
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• v.26 no.4
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• pp.18-23
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• 2012

After produce the extracted wood to silicic acid gel, sodium carbonate and silicon dioxide with application of the making method for carbon dioxide, ignition time, ignition temperature, mass loss rate and critical heat flux are measured according to external radiation source (20, 25, 35 and 50 $kW/m^2$). From the results, pressure impregnation wood to use with water glass and carbon dioxide has fire retardant performance at heat flux (less than 20 $kW/m^2$) of Pre-Flashover fires. If we find out the excellent maxing ratio through continuously study, it might be decided to be able to be utilized as fire-retardant wood.

• Journal of the Korean Society of Propulsion Engineers
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• v.23 no.2
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• pp.104-110
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• 2019

The thermal decomposition characteristics of boron-potassium nitrate ($BKNO_3$) were investigated by non-isothermal thermal gravimetric analysis (TGA). Two steps of mass loss were observed in the temperature range between room temperature and $600^{\circ}C$. Kinetic parameters of the thermal decompositions were evaluated from the measured TGA curves using the AKTS Thermokinetics Software. For the first step of mass loss ($220-360^{\circ}C$) corresponding to the thermal decomposition process of the binder (Laminac/Lupersol), the activation energy is in the range of approximately 120-270 kJ/mol when evaluated by Friedman's iso-conversional method, while the value of activation energy varies in the range of approximately 150-400 kJ/mol during the second step process ($360-550^{\circ}C$).