• 에너지공학
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• 제16권1호
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• pp.32-39
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• 2007

석탄 열분해 공정은 석탄의 종류와 산지에 따른 변화가 커서 반응특성을 석탄의 모든 종류에 일반화시키기는 어려우며, 열분해, 가스화 및 연소현상이 동시에 발생하므로 석탄의 종류에 따라 운전조건을 변화시켜 실험장치로부터 최적의 반응 조건을 찾는 것이 중요하다. 본 연구에서는 키데코탄을 대상으로 압력 $2kg_{f}/cm^{2}$ 온도 $735{\sim}831^{\circ}C$의 가압유동층 반응기에서 가스화 반응을 수행하였으며 스팀공급량, 석탄공급량, 공기공급량 등 실험 변수에 따른 가스화 반응의 변화를 관찰하였다. 또한 여러 실험변수들의 변화에 따른 생성가스 성분의 변화를 정량적으로 분석하고, 생성가스 중 $H_{2}$와 CO의 농도를 기준으로 최적의 반응 조건을 결정하였다. 본 실험에서의 최적의 반응 조건은 공기/석탄 비 4.45, 스팀/석탄 비 0.21이었다. 가스화 반응보다 연소반응이 활발하게 일어나면 반응온도가 급격히 증가하므로 안정적인 가스화를 위하여 석탄과 스팀의 주입속도 조절이 매우 중요하였다. 연속운전을 위한 안정적인 운전조건에서 생산되는 발생가스의 CO의 농도는 약 18%, $H_{2}$의 농도는 약 17%였다.

• 한국응용과학기술학회지
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• 제33권4호
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• pp.676-685
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• 2016

본 연구는 폴리스타렌(PS) 수지의 유화공정 효율성 향상을 위해 저온열분해 회분식 반응기를 이용하여, 단일 PS 수지와 Co 및 Mo 촉매를 각각 첨가한 PS 수지를 반응온도(425, 450, $475^{\circ}C$), 반응시간(20~80분, 15분 간격), 촉매 농도변화에 따른 PS수지의 액화생성물 전환율을 측정하였다. 최적의 열분해 조건은 반응온도 $450^{\circ}C$, 반응시간 35분으로 판단되며, 전환된 액화생성물의 주요 성분은 GC/MS 분석결과 스타이렌 및 벤젠유도체가 대부분으로 나타났다. 생성물은 산업통상자원부에서 고시한 증류성상 온도에 따라 가스, 가솔린, 등유, 경유, 중유로 분류하여 그 수율을 측정하였다. 그리고 $450^{\circ}C$ 반응온도에서 촉매 사용에 따른 전환율은 Co 촉매 > Mo 촉매 > 무촉매 순이었으며, 생성물 중 가스, 등유, 경유수율은 Mo 촉매, 가솔린은 무촉매, 중유는 Co 촉매에서 우수한 것으로 나타났다. Co 및 Mo 촉매 혼합 농도별 전환율 및 열분해 생성물 수율은 Co 촉매 100% 사용 시 가장 우수한 것으로 판단된다.

• 한국식품위생안전성학회지
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• 제6권1호
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• pp.57-66
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• 1991

참기름의 변조 여부를 쉽게 판별하고, 변조에 사용된 혼입유의 실태를 파악할 수 있는 방법으로써 FV(Fatty acid ratio & villavecchia reaction) value를 상요하였다. FV value 는 gas chromtography로 지방산 조성을 분석하여 C18: 1 + C18 : 2/C16 : $0{\times}C18$ : 3값을 구하고 이 값에 modified cilavecchia -suarez test(MVTV)에서 얻어진 값을 곱하여 결정하였다. 이 FV value를 이용하여 전남 지방 시장등지에서 구입한 참기름 총 74건에 대해 그 순도를 판별하고 변조에 사용된 혼입유의 실태를 파악하였다. 수거된 참기름들에 대해 FV value 로 산출한 결과 총 74건 중 11건만이 순수한 참기름으로 추정되어졌다. 변조에 상용된 혼입유의 실태를 산출된 FV value로 추정한 결과 대두유 혼입이 23건으로 가장 많았으며, 그밖에 미강유 혼입 및 깻묵을 유기용매로 재 추출한 참기름이 각각 10건, 들깨유 혼입이 8건, 옥수수유 혼입이 7건, 면실유 혼입이 3건, 채종유 혼입이 2건 등이었다.

• 한국표면공학회:학술대회논문집
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• 한국표면공학회 2016년도 추계학술대회 논문집
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• pp.156-156
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• 2016

The effect of nitrogen doping on the mechanical and tribological performance of single-layer tetrahedral amorphous carbon (ta-C:N) coatings of up to $1{\mu}m$ in thickness was investigated using a custom-made filtered cathode vacuum arc (FCVA). The results obtained revealed that the hardness of the coatings decreased from $65{\pm}4.8GPa$ to $25{\pm}2.4GPa$ with increasing nitrogen gas ratio, which indicates that nitrogen doping occurs through substitution in the $sp^2$ phase. Subsequent AES analysis showed that the N/C ratio in the ta-C:N thick-film coatings ranged from 0.03 to 0.29 and increased with the nitrogen flow rate. Variation in the G-peak positions and I(D)/I(G) ratio exhibit a similar trend. It is concluded from these results that micron-thick ta-C:N films have the potential to be used in a wide range of functional coating applications in electronics. To achieve highly conductive and wear-resistant coatings in system components, the friction and wear performances of the coating were investigated. The tribological behavior of the coating was investigated by sliding an SUJ2 ball over the coating in a ball-on-disk tribo-meter. The experimental results revealed that doping using a high nitrogen gas flow rate improved the wear resistance of the coating, while a low flow rate of 0-10 sccm increased the coefficient of friction (CoF) and wear rate through the generation of hematite (${\alpha}-Fe_2O_3$) phases by tribo-chemical reaction. However, the CoF and wear rate dramatically decreased when the nitrogen flow rate was increased to 30-40 sccm, due to the nitrogen inducing phase transformation that produced a graphite-like structure in the coating. The widths of the wear track and wear scar were also observed to decrease with increasing nitrogen flow rate. Moreover, the G-peaks of the wear scar around the SUJ2 ball on the worn surface increased with increasing nitrogen doping.

• 한국자동차공학회논문집
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• 제20권5호
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• pp.71-80
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• 2012

To improve the $NO_X$ conversion over a SCR (selective catalytic reduction) catalyst, the DOC (diesel oxidation catalyst) is usually placed upstream of the SCR catalyst to enhance the fast SCR reaction ($4NH_3+2NO+2NO_2{\rightarrow}4N_2+6H_2O$) using equimolar amounts of NO and $NO_2$. Here, a ratio of $NO_2/NO_X$ above 50% should be avoided, because the reaction with $NO_2$ only ($4NH_3+4NO+O_2{\rightarrow}4N_2+6H_2O$) is slower than the standard SCR reaction ($4NH_3+4NO+O_2{\rightarrow}4N_2+6H_2O$). In order to accurately predict the performance characteristics of SCR catalysts, it is therefore desired to develop a more simple and reliable mathematical and kinetic models on the oxidation kinetics of nitric oxide over a DOC. In the present work, the prediction accuracy and limit of three different chemical reaction kinetics models are presented to describe the chemicophysical characteristics and conversion performance of DOCs. Steady-state experiments with DOCs mounted on a light-duty four-cylinder 2.0-L turbocharged diesel engine then are performed, using an engine-dynamometer system to calibrate the kinetic parameters such as activation energies and preexponential factors of heterogeneous reactions. The reaction kinetics for NO oxidation over Pt-based catalysts is determined in conjunction with a transient one-dimensional (1D) heterogeneous plug flow reactor (PFR) model with diesel exhaust gas temperatures in the range of 115~$525^{\circ}C$ and space velocities in the range of $(0.4{\sim}6.5){\times}10^5\;h^{-1}$.

• 한국응용과학기술학회지
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• 제21권3호
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• pp.225-230
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• 2004

Synthesis gas is a high valued compound as a basic chemicals at various chemical processes. Synthesis gas is mainly produced commercially by a steam reforming process. However, the process is highly endothermic so that the process is very energy-consuming process. Thus, this study was carried out to produce synthesis gas by the partial oxidation of methane to decrease the energy cost. The effects of reaction temperature and flow rate of reactants on the methane conversion, product selectivity, product ratio, and carbon deposition were investigated with 13wt% Ni/MgO catalyst in a fluidized bed reactor. With the fluidized bed reactor, $CH_4$ conversion was 91%, and Hz and CO selectivities were both 98% at 850$^{\circ}C$ and total flow rate of 100 mL/min. These values were higher than those of fixed bed reactor. From this result, we found that with the use of the fluidized bed reactor it was possible to avoid the disadvantage of fixed bed reactor (explosion) and increase the productivity of synthesis gas.

• 대한전기학회:학술대회논문집
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• 대한전기학회 1999년도 하계학술대회 논문집 E
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• pp.2007-2009
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• 1999

In this paper, discharge domain of wire-cylindrical plasma reactor was separated from a gas flow duct to avoid unstable discharge by aerosol particle deposited on discharge electrode and grounded electrode. The NOx, SOx removal was experimentally investigated by a reaction induced to ammonium nitrate, ammonium sulfate using a low price of aqueous NaOH solution and a small quantity of ammonia. Volume percentage of aqueous NaOH solution used was 20% and $N_2$ flow rate was 2.5[$\ell$/min] for bubbling aqueous NaOH solution. Ammonia gas(14.82%) balanced by argon was diluted by air and was introduced to a main simulated flue gas duct through $NH_3$ injection system which was in downstream of reactor. The $NH_3$ molecular ratio[MR] was determined based on $NH_3$ to [NO+$SO_2$]. MR is 1.5. The NOx removal rates increased in the order of DC, AC and pulse, but SOx removal rates was not significantly effected by source of electricity. The NOx removal rate slightly decreased with increasing initial concentration but SOx removal rate was not significantly effect by initial concentration, and NOx, SOx removal rates decreased with increasing gas flow rate.

• 한국연소학회지
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• 제4권1호
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• pp.1-15
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• 1999

In order to analyze the sensitivity on the pulverized coal flames of the several variables, a numerical study was conducted at the gasification process. Eulerian approach is used for the gas phase, whereas lagrangian approach is used for the solid phase. Turbulence is modeled using the standard $k-{\varepsilon}$ model. The turbulent combustion incorporates eddy dissipation model. The radiation was solved using a Monte-Carlo method. One-step two-reaction model was employed for the devolatilization of Kideco coal. In pulverized flame of long liftoff height, the initial turbulent intensity seriously affects the position of flame front. The radiation heat transfer and wall heat loss ratio distort the temperature distributions along the reactor wall, but do not influence the reactor performance such as coal conversion, residence time and flame front position. The primary/secondary momentum ratio affects the position of flame front, but the coal burnout is only slightly influenced. The momentum ratio is a variable only associated with the flame stabilization such as flame front position. The addition of steam in the reactor has a detrimental effect on all the aspects, particularly reactor temperature and coal burnout.

• 한국세라믹학회지
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• 제31권5호
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• pp.552-560
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• 1994

A composite of TiB2-Al2O3 system was successfully prepared from a mixture of TiO2, B2O3, and Al by self-propagating high temperature synthesis (SHS) with a novel characteristic, utilizing the internal oxidation heat of aluminium metal of the mixture, instead of by a conventional technique, externally heating a mixture of Ti, B and Al2O3. From a mixture with B/Ti molar ratio of =2.0, pure two phases of TiB2 and $\alpha$-Al2O3 with good crystallinity and small, uniform sizes were formed. However, when the B/Ti molar ratio of the mixture goes to a value less than 2.0, in addition to the above main minerals, a small smounts of metastable phases such as TiB and Ti3B4 were formed. It was found that about 60%, the optimum green density of compacts gave their highest reaction rate and temperature during SHS process. TiB2-Al2O3 system composite with B/Ti molar ratio of =2.0 could be pressurelessly sintered even at 190$0^{\circ}C$ under Ar gas flows without any addition of sintering aids, showing their good properties such as 91.2% in relative density, 2750 kgf/$\textrm{mm}^2$ in Vickers hardness and 2620 kgf/$\textrm{cm}^2$ in flexural strength.

• Korean Chemical Engineering Research
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• 제53권6호
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• pp.818-823
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• 2015

본 연구에서는 전산유체역학(CFD)을 이용하여 마이크로채널 내부의 Fischer-Tropsch(FT) 반응을 모사하였고, 나아가 반응채널의 너비와 높이, 냉각채널과의 거리 그리고 채널 사이 간격을 변수로 두고 채널 내부 온도에 대해 민감도 분석을 수행하였다. 마이크로채널 반응기는 채널 간의 열교환을 고려하기 위한 5개의 반응채널과 냉각채널을 대신한 냉각면으로 이루어져 있으며 채널의 높이와 너비를 포함한 변수들의 길이는 0.5 mm ~ 5.0 mm 범위에서 설정하였다. 반응물로는 $H_2$와 CO의 혼합기체($H_2/CO$ molar ratio=2)를 사용하였으며 반응기의 운전 조건은 $GHSV=10000h^{-1}$, 압력 20 bar와 온도 483 K($210^{\circ}C$)이다. 민감도 분석의 결과로 반응채널 내부의 최대 온도는 채널의 높이에 비례하며 너비에 대해서는 특정 길이 이상에서 영향을 받지 않는 것을 확인하였으며 이 중에 냉각채널과의 거리와 채널 사이 간격은 채널 내부 온도에 거의 영향을 미치지 않았다. 따라서 채널 레이아웃에서 반응채널의 높이는 짧을수록(약 2 mm 이하), 너비는 길수록(약 4 mm 이상) 열제거뿐만 아니라 생산량 측면에서 이득을 얻을 수 있었다.