• 한국식품위생안전성학회지
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• 제13권3호
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• pp.206-212
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• 1998

Salmonella spp.의 신속한 검출을 위하여 엷은 박막형태의 수정결정을 사용하는 압전류적(piesoelectric) 항체센서 시스템을 개발하고 증류수, 완충용액, 식염용액 등의 여러 매질 중에서 보여주는 진동 특성을 검토하였다. Salmonella spp. 균 구조항원(Common structural antigen)에 대한 항체를 수정결정에 PEI pre-coating, BSA 가교화, 3-APTES silanizaition, protein A와 DTBP thiolation의 5가지 방법에 의해 고정화한 후 항체 센서의 안정성을 살펴보았다. Salmonella 균을 주입하였을 때 Salmonella 균과 수정 결정에 고정화한 항체와의 결함반응에 의해 수정결정의 질량증가와 이에 따른 진동수 감소가 나타났다. 고정화방법 중 protein A와 DTBP를 이용하여 고정화하는 방법이 센서반응을 가장 안정적이고 재현성 있게 나타내줌을 알 수 있었다. $7.45{\times}10^{7}\;CFU/ml$의 Salmonella 균을 반응 cell 내에 주입하였을 때 protein A를 이용한 고정화의 경우 80Hz, DTBP를 이용한 고정화의 경우 283 Hz의 진동수 감소가 나타났으며, 압전류적 항체센서를 이용할 경우 40분 이내에 Salmonella spp.의 검출이 가능하였다.

• KSBB Journal
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• 제22권6호
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• pp.443-446
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• 2007

관상심장질환 바이오마커의 하나인 CRP를 batch형 수정진동자 면역센서에 의하여 다음과 같이 분석하였다. 센서시스템의 작동은 직접결합방식에 의하여 행하였으며 CRP에 대한 항체의 최적 고정화농도는 $50{\mu}g/ml$이었다. 시스템의 반응완충용액으로 0.1 M 인산완충용액 (pH 7.0)을 사용하였고 시스템 작동은 baseline 안정화, 시료첨가 및 측정, 10 mM NaOH에 의한 센서 칩 재생의 순으로 행하였다. 이중로그척도로 표시하였을 때 0.27-106.00 nM 범위의 쥐 유래 CRP에 대하여 센서반응과 직선상의 관계를 이루었으며 센서의 검출한계는 0.53 nM이었고 재사용성도 양호하였다.

• 한국전기전자재료학회:학술대회논문집
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• 한국전기전자재료학회 2007년도 하계학술대회 논문집 Vol.8
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• pp.48-48
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• 2007

P-type transparent conducting $CuGaO_2$ thin films have been prepared by DC/RF sputtering using Quartz(0001) and sapphire(0001) substrates. The target was fabricated by heating a stoichiometric mixture of CuO and $Ga_2O_3$ at 1373K for 12h under $N_2$ atmosphere. The film were deposited under mixture gas of Ar and $O_2(Ar:O_2=4:1)$ during 10~30min. and the as-deposited films were annealed at 1123K and $N_2$ atmosphere. Room temperature conductivity and the activation energy of the sintered body in the temperature range of 223K ~ 423K were 0 004S/cm, 1.9eV, respectively. XRD revealed that all of the as-deposited films were amorphous. Heating of the films deposited on Quartz substrates above 1123K resulted in crystallization with a second phase of $CuSiO_3$, which was assumed owing to reaction with Quartz substrate. The single phase of $CuGaO_2$ was obtained at the film deposited on the sapphire substrates. The transmittance after annealing of DC- and RF-sputtered films were 55~75% at 550nm. From the transmittance and reflectance measurement. the direct band gap of the DC/RF-sputtered films were 3.63eV and 3.57eV. and there was little difference between DC and RF sputtered films.

• 자원환경지질
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• 제22권3호
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• pp.277-283
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• 1989

For the study of attenuation phenomena of the radioactive elements in solution, the adsorption experiment of thorium, uranium, barium and strontium on kaolinite, gibbsite, quartz, granite and shale as a function of time, pH and the surface area was conducted under the competition condition each other. There are two steps of adsorption kinetics. The first step is faster and completes in hours or a day, and the second step is slower eqiulibrium reaction. The adsorption rate which is considered to be related to CEC differs with adsorbent and decreases in the order of shale, kaolinite, granite, gibbsite and quartz. On the other hand, the adsorption rate for the same adsorbent differs with elements in the order of thorium,uranium, barium and strontium in decreasing rate. It is also affected by pH of the solution and the surface area of adsorbent. In conclusion, we didn't find any different between noncompetition condition and competition condition, and this means that we only have to consider the pH of ground water, the characteristics of the geological materials and the kinds of radioactive element in the case of selection of the places for the radioactive waste disposal.

• 한국결정성장학회지
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• 제10권4호
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• pp.309-317
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• 2000

Langasite is a promising new piezoelectric material for SAW filter application. Little was known until recently about the methods needed to mechanically polish and chemically polish/etch this material. In this experiment, polishing, slurry chemistry and chemical wet etching for langasite is described. Conventional quartz and LN ($LiNbO_3$) polishing methods did not produce satisfactory polished surfaces, and polishing with a colloidal silica slurries has shown to be most effective. The optimum condition was investigated by changing the slurry chemistry. As the planarization effect is very important in SAW filter applications, the examination of the effective particle number effect and the particle size effect was carried out. Z-cut langasite surface which had been polished with the colloidal silica slurries was etched in a variety of etchants. Conventional quartz etchants destroyed the polished surface. Other etchants formed a thin film on the surfaces. In this experiment, the reaction between langasite and a few etching solution was analysed. And an appropriate selective etchant solution for analyzing the defects was synthesized.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2005년도 춘계학술대회
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• pp.284-287
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• 2005

A fluidized bed reactor made of quartz with 0.055 m I.D. and 1.0 m in height was employed for the thermocatalytic decomposition of methane to produce $CO_2 - free$ hydrogen. The fluidized bed was proposed for the continuous withdraw of product carbons from the reactor. The methane decomposition rate with the carbon black N330 catalyst was quickly reached a quasi-steady state rate and remained for several hour. The methane decomposition reaction was carried out at the temperature range of $850-925^{\circ}C$, methane gas velocity of $1.0U_{mf}\;3.0U_{mf}$ and the operating pressure of 1.0 atm. Effect of operating parameters such as reaction temperature, gas velocity on the reaction rates was investigated. The produced carbon by the methane decomposition was deposited on the surfaces of carbon catalysts and the morphology was observed by SEM image.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 춘계학술대회
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• pp.81-85
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• 2007

A fluidized bed reactor is made with quartz. The size of FBR is 0.055 m I.D. and 1.0 m in height. The FBR was employed for the thermocatalytic decomposition of propane to produce hydrogen without $CO_{2}$. The fluidized bed was proposed for the continuous withdraw of product carbons from the reactor. Carbon black DCC-N330 is used to decompose the propane gas. The propane decomposition reaction over carbon black catalyst in a fluidized bed reactor was carried out the temperature range of 600 ${\sim}$ 800 $^{\circ}C$, propane gas velocity of 1.0 ${\sim}$ 4.0$U_{mf}$($1U_{mf}$ = 0.61cm/s) and the catalyst loading of 100 ${\sim}$ 200g. Production of $H_{2}$ such as other reaction temperature, gas velocity, catalytic loading on the reaction rates was investigated. The carbon depositied on the catalyst surface was observed by FE-SEM. The particle size of the carbon black was observed by Particle size analyzer. Resulting production in the experiment was not only hydrogen but also several by-products such as methane, ethylene, ethane, and propylene.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 춘계학술대회
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• pp.57-60
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• 2007

A fluidized bed reactor made of quartz with 0.055 m I.D. and 1.0 m in height was employed for the thermocatalytic decomposition of methane to produce $CO_{2}$ - free hydrogen. The fluidized bed was proposed for the continuous withdraw of product carbons from the reactor. The methane decomposition rate with the carbon black N330 catalyst was quickly reached a quasi-steady state rate and remained for several hour. The methane and propane mixture decomposition reaction was carried out at the temperature range of 850 - 900 $^{\circ}C$, methane and propane mixture gas velocity of 1.0 $U_{mf}$ ${\sim}$ 3.0 $U_{mf}$ and the operating pressure of 1.0 atm. Effect of operating parameters such as reaction temperature, gas velocity on the reaction rates was investigated. The produced carbon by the methane decomposition was deposited on the surfaces of carbon catalysts and the morphology was observed by SEM image.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2006년도 추계학술대회
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• pp.388-391
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• 2006

A fluidized bed reactor made of quartz with 0.055m I.D. and 1.0m in height was employed for the thermocatalytic decomposition of propane to produce $CO_2-free$ hydrogen. The fluidized bed was proposed for the continuous withdraw of product carbons from the reactor The propane decomposition rate used carbon black DCC-N330, Hi-900L as a catalyst. The propane decomposition reaction was carried out at the temperature range of $600-800^{\circ}C$, propane gas velocity of $1.0U_{mf}$ and the operating pressure of 1.0 atm. Effect of operating parameters such as reaction temperature on the reaction rates was investigated. Resulting production in our experiment were not only hydrogen but also several by products such as methane, ethylene, ethane, and propylene.

• 한국응용과학기술학회지
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• 제24권3호
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• pp.296-300
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• 2007

This paper presents applicability of photocatalytic decomposition of methyl mercaptan using $TiO_2$. A quartz reactor was used in order to elucidate reaction pathway in photocatalytic decomposition of methyl mercaptan. Experimental results showed that more than 99.9% of methyl mercaptan was decomposed within 30 minutes. It was found that the photocatalytic decomposition of methyl mercaptan followed pseudo first order and its reaction coefficient was $0.05min^{-1}$ During 30 minutes in the photocatalytic reaction, the concentration of methyl mercaptan, dimethyl disulfide, $SO_2$, $H_2SO_4$, COS, $H_2S$ were determined. These results showed that 64% of methyl mercaptan were compensated for the increase in sulfur after 30 minutes through the mineralization. The proposed main photocatalytic decomposition pathway of methyl mercaptan was methyl $mercaptan{\rightarrow}dimethyl$ $disulfide{\rightarrow}SO_2{\rightarrow}H_2SO_4$.