• 한국수소및신에너지학회논문집
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• 제18권2호
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• pp.171-181
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• 2007

Blending effects of hydrogen and water vapor on flame structure and NOx emission behavior are numerically studied with detailed chemistry in methane-air counterflow diffusion flames. The composition of fuel is systematically changed from pure methane and pure hydrogen to the blending fuels of methane-hydrogen-water vapor through the molar addition of $H_2O$. Flame structure is changed considerably for hydrogen-blending methane flames and hydrogen-blending methane flames diluted with water vapor in comparison to pure methane flame. These complicated changes of flame structures also affect NOx emission behavior considerably. The changes of thermal NO and Fenimore NO are analyzed for various combinations of the fuel composition. Importantly contributing reaction steps to thermal NO and Fenimore NO are addressed in pure methane, hydrogen-blending methane flames, and hydrogen-blending methane flames diluted with water vapor.

• 한국응용과학기술학회지
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• 제24권2호
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• pp.140-148
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• 2007

As an additional high purification method of p-dioxanone monomer for a high molecular weight polymer, the sweating operation of crystalline layer obtained by layered melt crystallization from p-dioxanone-diethylene glycol system was studied. Purity and yield of p-dioxanone crystal depended mainly on the sweating temperature and sweating time. Increasing sweating time and sweating temperature, the purity of p-dioxanone crystal increase, whereas the yield of that decrease, respectively. Through the optimization of sweating operation, p-dioxanone crystal can be upgraded to very high purity over 99.9 % suited to monomer for polymerization.

• 한국응용과학기술학회지
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• 제24권3호
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• pp.219-232
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• 2007

In T-mixer crystallization, supersaturation is generated by mixing of another solvent or non-solvent in order to reduce the solubility of the compound. Also, T-mixer is a type of continuous crystallization. In order to induce micro-mixing, two solutions were mixed rapidly by T-mixer, which formed high supersaturation. As the results, mean size of HMX crystals decreased with increasing de-supersaturation rate $(R_s)$. Eventually, HMX particles ranging from 0.5 to $5{\mu}m$ can be obtained by T-mixer crystallization. Mixing efficiency in T-mixer increased with increasing $R_s$ values. In T-mixer crystallization without surfactants, homogeneous nucleation was formed when S and $R_s$ was over 54 and $1.6{\times}10^3/sec$. In T-mixer crystallization with surfactants, homogeneous nucleation was formed when S and $R_s$ was over 26 and 7.4/sec.

• 한국응용과학기술학회지
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• 제24권4호
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• pp.383-392
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• 2007

This paper is studied on the efficient purification process of dimethyl carbonate (DMC) from the melt layer crystallization combining crystallization process, sweating process and distillation recovery process. Purity and yield of DMC crystal depended mainly on the crystallization temperature, cooling rate, sweating termperature sweating rate. Through the optimization of crystallization and sweating operation, DMC crystal can be upgraded to very high purity over 99.9% and high yield over 85%.

• 설비공학논문집
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• 제18권11호
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• pp.851-858
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• 2006

[ $CO_2$ ] and propane mixtures, which are environmentally benign, nontoxic, low in price, and compatible with materials and lubricants, were considered as promising alternative refrigerants. A fully instrumented air-conditioning system was developed for a precise performance evaluation of pure $CO_2$ and $CO_2/propane$ mixtures. In this paper, the effect of the charging amount and circulation concentration on the cooling performance of the system using $CO_2$ and propane mixtures was tested and discussed. Pure $CO_2$ and 85/15, 75/25 and 60/40 binary blends by the charged mass percentage of $CO_2/propane$ were selected as working fluids. An optimum charging amount was proposed as a parameter instead of the degree of subcooling, which can not be well defined in the transcritical cycle, to properly compare the performance between the transcritical and subcritical cycles.

• Membrane and Water Treatment
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• 제13권4호
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• pp.191-199
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• 2022

In industrial production, the development of traditional polyamide nanofiltration (NF) membrane was limited due to its poor oxidation resistance, complex preparation process and high cost. In this study, a composite NF membrane with high flux, high separation performance, high oxidation resistance and simple process preparation was prepared by the method of dilute solution dip coating. And the sulfonated polysulfone was used for dip coating. The results indicated that the concentration of glycerin, the pore size of the based membrane, the composition of the coating solution, and the post-treatment process had important effects on the structure and performance of the composite NF membrane. The composite NF membrane prepared without glycerol protecting based membrane had a low flux, when the concentration of glycerin increased from 5% to 15%, the pure water flux of the composite NF membrane increased from 46.4 LMH to 108.2 LMH, and the salt rejection rate did not change much. By optimizing the coating system, the rejection rate of Na₂SO₄ and PEG1000 was higher than 90%, the pure water flux was higher than 40 LMH (60psi), and it can withstand 20,000 ppm.h NaClO solution cleaning. When the post treatment processes was adjusted, the salt rejection rate of NaCl solution (250 ppm) reached 45.5%, and the flux reached 62.2 LMH.

• 한국재료학회지
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• 제16권2호
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• pp.106-110
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• 2006

We have investigated the effect of the experimental variables such as temperature and pressure on conformality of Co films deposited over high aspect ratio trenches using $Co_2(CO)_8$ as a precursor. The results show that the conformality of Co films is a strong function of temperature and process pressure. Lowering the pressure and temperature significantly improves the conformality. As the pressure decreases from 0.6 Torr to 0.2 Torr at $50^{\circ}C$, the bottom coverage of Co films over $0.2{\mu}m$ width trenches with an aspect ratio of 13 to 1 significantly increases to 85%. However, further increasing the temperature from 50 to $60^{\circ}C$ at the pressure of 0.2 Torr degrades the bottom coverage to 14%. In contrast, the extremely low pressure of 0.03 Torr allows the excellent conformal deposition of Co films up to $70^{\circ}C$. This can be attributed to the suppression of homogeneous reaction in the gas phase, which can create the intermediate products with high sticking coefficient. In addition, the Co films deposited at $50^{\circ}C$ show the low resistivity with negligible contamination. As a result, the newly developed Co process using MOCVD can be implemented into the next generation devices with complex shapes.

• 한국해양학회지:바다
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• 제18권1호
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• pp.40-46
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• 2013

안정동위원소 질량분석기를 이용한 탄소와 산소의 동위원소비 측정은, 이산화탄소 표준기체의 동위원소 비에 대하여 그 상대적인 값을 측정함으로써 이루어진다. 따라서 실험실 표준기체는 ${\delta}^{13}C$와 ${\delta}^{18}O$ 값의 국제 표준물질인 PDB와 V-SMOW에 대해 보정된 이산화탄소이여야 하며, 이는 국제적 자료의 비교와 검증을 위해 필수적이다. 그러나 표준기체는 제작 기간이 길며, 가격이 비싼 단점이 있고, 장기간 사용 시 실린더 내부 압력의 변화로 동위원소의 분별이 생길 우려가 크다. 따라서 본 연구는 실험실 표준기체 관리의 효율성을 높이기 위해 장기간 안정적 보관이 가능한 고체 표준물질로부터 동위원소 분별없이 순수한 이산화탄소 기체를 추출하여, 실험실 표준기체로 사용할 수 있는 방법을 제시하고자 한다. 본 논문은 Coplen et al.(1983)에 의하여 제안된 방법을 기초로 한 다량의 이산화탄소 표준 기체 제작에 초점을 두었다. 이산화탄소는 탄산칼슘과 100% 순수 인산의 반응에 의해 생성되는데, 두 물질의 반응에 필요한 실험 장치 및 실험 과정을 상세히 기술하였으며, 최적의 실험 조건 결정을 위한 다양한 분석 결과를 소개하였다. 이어 생성된 이산화탄소 기체의 추출, 정제와 포집은 자체 제작된 진공관에서 이루어졌으며, 각 단계에 대한 자세한 설명이 주어진다. 이산화탄소의 ${\delta}^{13}C$와 ${\delta}^{18}O$ 측정은 서울대학교 기초과학교육연구 공동기기원에서 운영 중인 안정동위원소 질량분석기(VG Isotech, SIRA Series II)를 이용하여 이루어졌다. 탄산칼슘 고체 표준물질로부터 이산화탄소 기체 추출과 추출된 기체의 정제 포집 등 전체 분석과정의 정밀도 검증을 위해 동일한 Solenhofen-ori $CaCO_3$(< $63{\mu}m$) 고체 시료로 부터 15회에 걸쳐 표준기체를 제작하였고, 매회 100 mg $CaCO_3$을 이용하여 총 15개의 표준기체 제작이 8일에 걸쳐 이루어졌다. 이 표준기체들의 분석 표준편차($1{\sigma}$)는 ${\delta}^{13}C$의 경우 ${\pm}0.01$‰, ${\delta}^{18}O$는 ${\pm}0.05$‰로 매우 높은 정밀도를 보여주었다. 이러한 분석 정밀도는 안정동위원소 질량분석기기 자체와 같은 내부 정밀도에 상응하며, 본 연구에서 제시한 실험실 표준기체 제작방법의 높은 신뢰성과 재현성을 입증하는 결과이다. 따라서 본 연구는 표준기체 보유가 어려워 정밀, 정확한 안정동위원소 분석에 어려움이 많았던 연구 분야에 자체 표준기체 제작 기술을 제공하는데 크게 기여할 것으로 생각된다.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 1997년도 추계학술대회 논문집
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• pp.347-349
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• 1997

In order to investigate CO sensing property of a SnO$_2$-WO$_3$composite ceramic. we prepared pure SnO$_2$and WO$_3$added SnO$_2$compostie ceramics. Using XRD and SEM, a phase analysis and microstructure were investigated. The resistances as a function of gas atmosphere were measured by High Voltage Measure/source Unit. The measured 1000ppm CO gas sensitivity of SnO$_2$-WO$_3$composite ceramics were smaller than that of pure SnO$_2$.

• 한국표면공학회지
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• 제37권1호
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• pp.28-39
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• 2004

The effect of trace metallic additives on microstructure, surface appearance and hardness of zinc electrodeposits was investigated by using sulfate bath and flow cell system. The preferred orientation of Zn deposit with Fe additive was (103)(104)+(002) mixed texture and that of Zn deposits with both Fe-Ni and Fe-Co additives was (10 1), while Zn deposits with Fe-Cr additives had (002) preferred orientation. The surface morphology of the zinc deposits was closely related to the preferred orientation of the deposits. The glossiness of Zn deposit with Fe-Ni additives was higher than that of pure Zn deposit, while the glossiness of Zn deposits with both Fe-Co and Fe-Cr additives was lower than that of pure Zn deposit. The hardness of Zn deposits with both Fe-Ni and Fe-Co additives was noticeably higher than that of Zn-Fe deposit, while that of Zn deposit with Fe-Cr additives was similar to that of Zn-Fe deposit.