• Korean Chemical Engineering Research
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• 제47권3호
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• pp.292-302
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• 2009

페놀 습식산화에 미치는 반응온도($150{\sim}250^{\circ}C$), 산소분압(25.8~75.0 bar) 및 초기 pH(1.0~12.0)의 영향을 10 g/l의 페놀 초기농도를 사용하여 조사하였다. 습식산화속도는 화학적 산소요구량 COD를 이용하여 산출하였으며 반응 중간 생성물들을 고성능액체크로마토그래피를 사용하여 측정하였다. 습식산화 중 페놀 분해속도는 페놀에 대하여 1차 반응차수를 나타냈으며, COD 변화는 lumped 모델로 잘 묘사할 수 있었다. 금속이온($Cu^{2+}$, $Fe^{2+}$, $Zn^{2+}$, $Co^{2+}$, $Ce^{3+}$) 균일촉매의 습식산화 중 페놀 분해속도 및 COD 제거속도에 미치는 영향도 조사하였다. 페놀 분해속도 및 COD 제거속도는 $CuSO_4$를 사용한 촉매습식산화에서 가장 크게 나타났으며 촉매농도를 증가시킴에 따라 증가하였다. 습식산화 중 생성되는 개미산의 분해속도는 반응온도 및 $CuSO_4$ 농도를 증가시킴에 따라 증가하였다. 난분해성 생성물 초산의 최종농도는 반응온도를 증가시킴에 따라 증가하였으나 $CuSO_4$ 농도를 증가시킴에 따라 감소하였다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2010년도 추계학술대회 초록집
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• pp.115.2-115.2
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• 2010

Autothermal reforming(ATR) processes of hydrocarbon liquids such as diesel fuels are spotlighted as methods to produce hydrogen for Fuel cell. However, the use of heavy hydrocarbons as feedstocks for hydrogen production causes some problems which increase the catalyst deactivation by the carbon deposition. Coking can be inhibited by increasing the water dissociation on the catalyst surface. This results in catastrophic failure of whole system. Performance degradation of diesel autothermal reforming leads to increase of undesirable hydrocarbons at reformed gases and subsequently decrease the performance. In this study, perovskite-based catalysts were investigated as alternatives to substitute the noble metal catalyst for the ATR of diesel. The investigated perovskite structure was based on LaCrO3. and metals were added at the A-site to enhance oxygen ion mobility, transition metals were doped on the B-site to enhance the reformation. Substituted Lanthanum chromium perovskite were made by aqueous combustion synthesis, which can produce high surface area. And for the homogeneous fuel supply, we made ultrasonic injection system for reforming. We compared durability of evaporation system and ultrasonic system for fuel injection.

• Advances in Energy Research
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• 제4권4호
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• pp.325-337
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• 2016

Cerbera Odollam (sea mango) is a proven promising feedstock for the production of biodiesel due to its high oil content. Fatty acid methyl esters (FAME) were produced as the final reaction product in the transesterification reflux condensation reaction of sea mango oil and methyl acetate (MA). Potassium methoxide was used as catalyst to study its reacting potential as a homogeneous base catalyst. The initial part of this project studied the optimum conditions to extract crude sea mango oil. It was found that the content of sea mango sea mango oil was 55%. This optimum amount was obtained by using 18 g of grinded sea mango seeds in 250 ml hexane. The extraction was carried out for 24 hours using solvent extraction method. Response surface methodology (RSM) was employed to determine the optimum conditions of the reaction. The three manipulated variables in this reaction were the reaction time, oil to solvent molar ratio, and catalyst wt%. The optimum condition for this reaction determined was 5 hours reaction time, 0.28 wt% of catalyst and 1:35 mol/mol of oil: solvent molar ratio. A series of test were conducted on the final FAME product of this study, namely the FTIR test, GC-FID, calorimeter bomb and viscometer test.

• 한국세라믹학회지
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• 제24권6호
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• pp.561-571
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• 1987

In case of glass ceramics and powder preparation from the metalakoxide solutions, metalakoxide solutions with a various species of alkoxy groups have unique characteristics. Therefore, in this study, the mixing ability of homogeneous sol, gel morphology and physical properties of gels were investigated by the changes in terms of the different four alkoxy groups, CH3-, C2H5-, i-C3H7-n-C4H9-, along with the catalyst for the purpose of the observation about the homogenous transition range from sol to gel. As a result, when the fixed condition was mol ratio of H2O/Si(OR)4=2.0 and variables were batch composition and addition amount of catalyst, the characteristics of Tetra-normal-Butoxysilane and Tetra-iso-propoxysilane systems had very narrow sol-gel conversion region than Tetramethoxysilane and Tetraethoxysilane system. And silicon-alkoxide, systems having narrow sol-gel conversion region were enlarged by addition of catalyst. In viewpoint of the weight loss of gel produced by hydrolysis of silicon alkoxide systems with different four alkoxy groups, the amounts of weight loss of gel containing large molecular alkoxy groups were much more than those of small molecular alkoxy group.

• 대한환경공학회지
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• 제29권1호
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• pp.62-67
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• 2007

본 연구의 목적은 액상 균일질 촉매를 이용하여 연소가스 중에 포함되어 있는 $SO_2/NO$의 동시제거 기술 개발에 있다. 연구는 bench scale/소규모 pilot scale에서 이루어졌으며 연구 결과는 다음과 같다. 1) $SO_2$는 실험조건에 상관없이 높은 제거효율을 가지는 것으로 확인되었다. 그러나 NO의 경우 충진층 높이가 증가할수록, 농도가 낮을수록, 촉매 분사량이 증가할수록 제거효율이 증가하는 것으로 나타났다. 2) Fe(II)-EDTA를 이용한 $SO_2/NO$ 동시처리 기술 개발을 위한 최적의 설계 인자는 충진 높이 =0.5 m, 액체-기체비 = 20 $L/m^3$, 반응기 단수=3단, 반응기 단면적 = 0.025 $m^2$로 결정하였다. 3) 연구 결과를 기초로 $SO_2/NO$의 동시처리 효율을 실험한 결과 각각 95%, 81% 이상 제거가 가능했다. 4) 높은 HTU는 NO의 제거에 있어 유리하지만 과도한 HTU는 스크러버의 운전효율을 감소시키므로 최적의 HTU를 결정하는 것이 필요하다.

• Korean Chemical Engineering Research
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• 제43권5호
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• pp.621-626
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• 2005

Amberlyst-15 고체 산 촉매를 사용하여 올레산을 메탄올과 반응시켜 바이오 디젤의 성분이 되는 지방산 메틸 에스테르로 전환시켰다. 본 연구에서는 시료의 산가를 측정하고 전환율을 구함으로써 반응 온도, 메탄올 대 올레산의 몰 비 및 촉매의 양이 반응에 미치는 영향을 살펴보았다. 실험 범위 내에서 반응 온도가 $20^{\circ}C$ 상승할 때에 반응 속도는 약 2배씩 증가하였다. 그리고 메탄올 대 올레산의 몰 비가 증가 될 때는 최종 전환율은 증가하였지만, 반응에는 뚜렷한 차이가 없었다. 촉매 역시 반응에 중요한 변수로써, Amberlyst-15의 양을 2배로 증가시켰을 때, 반응속도는 1.2-1.3배 빨라졌다. 실험 데이터를 정량적으로 해석하기 위해 동역학식 연구를 하였으며 모사 균일 혼합물 모델(pseudo-homogeneous model)을 이용한 2차 반응 속도식을 전개하였다.

• 공업화학
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• 제24권1호
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• pp.55-61
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• 2013

$Cp_2ZrCl_2$ 촉매를 Montmorillonite (MMT) 담체에 각기 다른 3가지 방법[MMT/$Cp_2ZrCl_2$, MMT/MAO/$Cp_2ZrCl_2$, MMT/(MAO + $Cp_2ZrCl_2$)]을 적용하여 불균일 촉매를 제조하였고, 이를 이용하여 에틸렌 중합 특성을 조사하였다. 유기점토인 30B-MMT에 담지한 불균일계 촉매가 자연점토인 $Na^+-MMT$에 담지한 촉매보다 높은 담지율을 나타내었고, 에틸렌 중합에서 높은 활성을 보였다. 이는 유기점토의 층간사이에 존재하는 하이드록시기가 MAO 및 촉매와의 화학적 결합을 유도한다고 할 수 있다. MMT에 직접 메탈로센을 담지하여 에틸렌 중합에 사용할 경우 균일계 촉매에 비해 낮은 활성을 보이지만, MMT를 MAO로 처리해서 만든 MMT/MAO/$Cp_2ZrCl_2$ 촉매에 MMAO의 조촉매를 사용하여 중합시에는 높은 활성을 나타내었다. MMT 담지촉매로 제조된 폴리에틸렌은 담지방법에 관계없이 균일계 촉매에 비해 높은 용융점, 분자량, 분자량 분포를 보였으며, 또한 입자형상에 있어 크기가 상당히 증가한 구형의 입자를 나타내었다. 또한 가장 안정적인 담지 반응과 높은 활성을 나타낸 30B-MMT/MAO/$Cp_2ZrCl_2$ 촉매로 최적의 중합조건을 찾기 위해 공정변수에 따라 에틸렌 중합을 수행하였다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 춘계학술대회
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• pp.41-44
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• 2007

Steam reforming reaction of natural gas is an important process for fuelcell commercialization. In this paper, steam reforming reaction is studied by numerical method. Pseudo-homogeneous model is incorporated for chemical reactions and one medium approach is used to take into account thermally equilibrium phenomena between catalyst and bulk gas. The model is validated with our experimental results under the same operating conditions. Because performance of reformer has relation to heat flux from wall, heat flux profiles was investigated by using Nusselt number. Value of Nusselt number in steam reformer is larger than one in channel, which does not have chemical reaction because steam reforming reaction is an endothermic reaction. When the difference of Nusselt number at the front and the rear is larger, performance is improved.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2001년도 춘계학술대회논문집D
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• pp.989-994
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• 2001

Numerical simulations of high temperature catalytic combustion have been performed for the application to a gas turbine combustor. Dependences of inlet temperature and pressure on the distributions of temperature and species concentrations were investigated using plug flow model with detailed homogeneous and heterogeneous chemistries of methane-air mixtures. Honeycomb typecombustor deposited with Pt catalyst of 100mm in length and 26mm in diameter is used. The results show that rapid increase of temperature profile occurs earlier with the increase of inlet temperature and the decrease of inlet pressure. The condition which catalytic combustion is stabilized exists at certain range of inlet temperature and pressure. The state of catalytic combustion is also confirmed by the distributions of species concentration.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2007년도 추계학술대회 논문집
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• pp.113-116
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• 2007

Performance of a steam reformer can be improved by using a coaxial cylindrical reactor, because the design can enhance the heat transfer for the steam reforming reaction, which is the one of main rate-determining steps of overall reactions. The objective of this study is to investigate the coaxial cylindrical reactor numerically. Pseudo-homogeneous model and one medium approach are incorporated for the chemical reactions, and models are validated with experimental results. The catalyst of the coaxial cylindrical reactor is 67% for one of the cylindrical reactor, but fuel conversion of the coaxial cylindrical reactor is increased by 10%. Heat flux profiles are investigated by modified Nusselt number and heat flux which is transported from the product gas to the catalyst bed affecting performance of the steam reformer.