• Applied Chemistry for Engineering
• /
• v.24 no.5
• /
• pp.513-517
• /
• 2013

We investigated the properties of impregnated activated carbons, a commercial adsorbent for the individual protection equipment, and examined CO adsorption and oxidation to $CO_2$. The surface area, pore volume and pore size were measured for four commercial samples using Brunauer-Emmett-Teller/Barrett-Joyner-Halenda (BET/BJH), and atomic compositions of the sample surface were analyzed based on SEM/EDS and XPS. Impregnated activated carbons containing Mn and Cu for fire showed the catalytic CO oxidation to $CO_2$ with a high catalytic activity (up to 99% $CO_2$ yield), followed by the CO adsorption at an initial reaction time. On the other hand, C: for chemical biologial and radiological (CBR) samples, not including Mn, showed a lower CO conversion to $CO_2$ (up to 60% yield) compared to that of fire samples. It was also found that a heat-treated activated carbon has a higher removal capacity both for CO and $CO_2$ at room temperature than that of untreated carbon, which was probably due to the impurity removal in pores resulted in a detection-delay about 30 min.

• Journal of the Korean Vacuum Society
• /
• v.20 no.3
• /
• pp.182-188
• /
• 2011

Polysilazane and polymethylsilazane based precursor films were deposited on Si-substrate by spin-coating, subsequently annealed at $150{\sim}850^{\circ}C$, and characterized. Structural analysis, shrink, compositional change, etch rate, and gap-filling were observed. Annealing the precursor films led to formation of spin-on dielectric films. C-containing precursor films showed that less loss of N, H, and C while less gain of O than that of C-free precursor films at $400^{\circ}C$, but more loss of N, H, and C while more gain of O at $850^{\circ}C$. Thus polysilazane based precursor films exhibited less reduction in thickness of 14.5% than silazane based one of 15.6% at $400^{\circ}C$ but more 37.4% than 19.4% at $850^{\circ}C$. FTIR indicated that C induced smaller amount of Si-O bond, non-uniform property, and lower resistance to chemical etching.

• Proceedings of the Materials Research Society of Korea Conference
• /
• 2003.11a
• /
• pp.239-239
• /
• 2003

탄소재료의 산화반응을 설명한 대부분의 논문은 TGA(Thermo Gravimetric Analysis)를 이용한 연구이다. TGA 장치는 가열이 필요한 물질의 반응연구에 다양하게 이용되고 있는데, 온도에 대한 무게 변화를 간편하게 알 수 있다는 장점과 함께 보편적으로 편리한 Arrhenius형태의 속도식으로 해석된다. 많은 연구자들은 TGA를 이용하여 다양한 탄소재료에 대한 반응속도상수를 구하였으며, 반응기체, 반응온도 및 원료물질에 따라 다른 속도를 나타내는 실험결과를 표준화된 속도식으로 표현하고자 하는 노력이 있었다. 그러나 이런 대부분의 연구는 coal 등과 같은 탄소재료의 연소특성을 이용하려는 에너지 변환 연구가 주를 이루어 왔으며, 탄소섬유의 산화반응에 대한 표준화 식으로 해석한 보고는 거의 없는 실정이다. 이 연구에서는 내부구조가 현격하게 차이나는 다른 두 종류의 피치계 탄소섬유를 TGA를 이용하여 등온 산화반응 시켰다. 반응기체의 종류와 반응온도를 변화시켜 산화반응조건에 따른 중량변화를 관찰하였고, 여러 산화조건에서 얻어진 산화속도를 Kasaoka 등에 의해 제안된 표준화식을 이용하여 산화반응의 평균 속도상수 K와 전환율이 0.5일 때의 속도상수 $k_{f=0.5}$ 결과를 비교하여 산화 반응속도를 정량적으로 해석하고자 하였다.다.

• Proceedings of the KIEE Conference
• /
• 2011.07a
• /
• pp.1312-1313
• /
• 2011

IT 산업의 발전에 따른 디지털 부하 증가는 기존 교류 배전 방식에서 DC 전원 공급에 따른 전력 변환 손실을 야기시킨다. 또한, 향후 신재생에너지를 통한 발전원 및 전기자동차의 계통 유입 확대로 인해 AC/DC 전력 변환에 따른 손실은 더욱 증대될 것으로 예상된다. 이에 본 논문에서는 DC 전원 공급율에 따른 전력 공급량 산정 기법을 제안한다. 또한, 탄소배출 비용을 함께 고려하여 DC 전원 공급율에 따른 신재생에너지 계통 연계의 경제적 타당성을 분석한다.

• 한국신재생에너지학회:학술대회논문집
• /
• 2007.11a
• /
• pp.424-428
• /
• 2007

In the current most tool using heat and mass balance in a coal gasifier is dependent on commercial code such as STANJAN, CHEMKIN. However, in order to keep the self-reliance technology, it is necessary to develop the original design tool available for comprehension and analysis on the spot. So in this study, its own heat and mass balance program is developed on the assumption that the process in a coal gasifier is adiabatic and quasi-equilibrium. The mass balance is calculated by using the chemical equilibrium principle. Also the heat and mass balance according to main operating factors such as temperature, pressure and O2/Coal ratio, was carried in this tool. This heat and mass balance was verified on the basis of the results simulated in STANJAN, commercial codes using similar logic.

• Journal of the Korean Chemical Society
• /
• v.47 no.3
• /
• pp.213-219
• /
• 2003

The photochemical transformation of carbon monoxide in aqueous solution has been investigated at $25{\pm}0.1^{\circ}C$using ZnO as a photocatalyst. After irradiation of 253.7 nm UV light in the solution, carboxylation and carbonylation processes were carried out, and the formation of formic acid, oxalic acid, glyoxylic acid, formaldehyde and glyoxal was observed. The formation of the products depended on the pH values in the solution. The yield of formaldehyde and glyoxal increased in acidic solution whereas it decreased in basic solution. When the pH values in the solution increased above 11.5, the yield of formic acid increased rapidly. The initial quantum yields of the products were determined and the probable mechanisms for the reactions were presented on the basis of the products analysis.

• Resources Recycling
• /
• v.16 no.6
• /
• pp.34-38
• /
• 2007

For recycling of tantalum from obsolete condenser, physical separations and chlorination of tantalum scraps with $Cl_2$ and $CCl_4$ were investigated. The recovery ratio of tantalum from obsolete condenser was 98% by using a multidisciplinary process of crushing by stamp mill, wet gravity separation by the shaking table, and air classification. In the chlorination reaction of non-oxidized Ta anode with $Cl_2$, the highest weight loss ratio is at least 60%, while in the chlorination reaction of Ta anode with $CCl_4$, the reaction rate for the oxidized Ta anode is faster than that of the non-oxidized Ta anode.

• KSBB Journal
• /
• v.17 no.4
• /
• pp.376-380
• /
• 2002

Production of the exopolymer by Aureobasidium pullulans SM-2001, UV induced mutant of A. pullulans ATCC 42023, was investigated. The exopolymer produced by A. pullulans SM-2001 was confirmed to be ${\beta}$-1,3-linked homoglucans containing a few ${\beta}$-1,6-linked single glucosyl branches(${\beta}$-1,3/1,6-glucan) with the nuclear magnetic resonance(NMR) spectrum. The average molecular weight of ${\beta}$-1,3/1,6-glucan produced by A. pullulans SM-2001 was about 2.6 ${\times}$ 10$\^$5/ by the gel permeation chromatographic analysis. Sucrose was known to be better carbon source for the production of ${\beta}$ -1,3/1,6-glucan than other tested carbon sources in this study. Maximal conversion rate of ${\beta}$-1,3/1,6-glucan was about 50% when the carbon source was 0.5%(w/v) sucrose.

• Proceedings of the Korea Air Pollution Research Association Conference
• /
• 2000.04a
• /
• pp.145-146
• /
• 2000

미세입자는 폐포에 침착율이 높고 다환방향족탄화수소(PAHs)와 같은 독성이 강한 유기물질과 SO$_2$와 NOx 등의 무기가스들의 입자로의 변환으로 생성된 $H_2SO_4$, $NH_4HSO_4$ 및 ${(NH_4)}_3H{(SO_4)}_2$ 등의 산성 황산화물 등과 같은 산성오염물질도 다량 함유하고 있다. 이러한 산성오염물질은 기침 및 호흡기 기능 저하와 같은 인체에 여러 가지 악영향을 미치는 것으로 알려져 있다(강병욱, 1998). 또한 대기에서 시정장애에 주로 영향을 미치는 입자는 0.1~1.0$\mu\textrm{m}$인 미세입자이며 그들중 황산염, 질산염 및 탄소함유성분들이 시정장애에 크게 기여하는 것으로 보고된다. (중략)

• Clean Technology
• /
• v.25 no.2
• /
• pp.107-113
• /
• 2019

Numerical model that considered the shrinking core model and elutriation and degradation of particles was developed to predict selective chlorination of ilmenite and carbo-chlorination of $TiO_2$ in a two stage fluidized bed chlorination furnace. It is possible to analyze the fluidized bed chlorination reaction to be able to reflect particle distribution for mass balances and the chlorination reaction. The numerical model showed an accuracy with error less than 6% compared with fluidized bed experiments. The chlorination degree with particle size change was greater with a smaller particle size, and there was a 100 min difference to obtain a chlorination degree of 1 between $75{\mu}m$ and $275{\mu}m$. This was not shown to such a great extent with variation of temperature ($800{\sim}1000^{\circ}C$), and there was only a 10 min difference to obtain a chlorination degree of 0.9. In the first selective chlorination process, the mass reduction rate approached to the theoretical value of 0.4735 after 180 min, and chlorination changed the Fe component into $FeCl_2$ or $FeCl_3$ and showed nearly 1. In the second carbo-chlorination process, the chlorination degree of $TiO_2$ approached 0.98 and the mass fraction reached 0.02 with conversion into $TiCl_4$. In the first selective chlorination process, 98% of $TiO_2$ was produced at 180 min, and this was changed into 99% of $TiCl_4$ after an additional 90 min. Also the mass reduction rate of $TiO_2$ was reduced to 99% in the second continuous carbo-chlorination process.