• 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.

• 한국산학기술학회논문지
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• 제17권2호
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• pp.209-213
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• 2016

경유자동차의 질소산화물을 저감하기위한 원심유동층장치를 개발하기 위해, 가스분산판 내경 184mm, 폭 50mm의 원심유동층장치에서 평균입자직경 $26{\mu}m$, $32{\mu}m$의 Cu-ZSM-5 제오라이트 촉매를 유동입자로 사용하여 원심유동층의 유동특성을 조사한 결과, 원심유동층내의 기포직경은 거의 0.3~3.0mm의 작은 범위이며, 기포의 상승속도는 기포직경 및 가스속도와 상관없이 0.0~0.4m/s 정도이다. 또한 원심유동층에서 사용가능한 평균입자 직경은 $60{\mu}m$이며, 층내에서 기체와 고체의 접촉은 양호한 것으로 조사되었다.

• International Journal of Advanced Culture Technology
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• 제3권1호
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• pp.21-30
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• 2015

Ceramic foams are prepared as positive images corresponding to a plastic foam structure which exhibits high porosities (85-90%). This structure makes the ceramic foams attractive as a catalyst in a dry reforming process, because it could reduce a high pressure drop problem. This problem causes low mass and heat transfers in the process. Furthermore, the reactants would shortly contact to catalyst surface, thus low conversion could occur. Therefore, this research addressed the preparation of dry reforming catalysts using a sol-gel catalyst preparation via a polymeric sponge method. The specific objectives of this work are to investigate the effects of polymer foam structure (such as porosity, pore sizes, and cell characteristics) on a catalyst performance and to observe the influences of catalyst preparation parameters to yield a replica of the original structure of polymeric foam. To accomplish these objectives industrial waste foams, polyurethane (PU) and polyvinyl alcohol (PVA) foams, were used as a polymeric template. Results indicated that the porosity of the polyurethane and polyvinyl alcohol foams were about 99% and 97%. Their average cell sizes were approximate 200 and 50 micrometres, respectively. The cell characteristics of polymer foams exhibited the character of a high permeability material that can be able to dip with ceramic slurry, which was synthesized with various viscosities, during a catalyst preparation step. Next, morphology of ceramic foams was explored using scanning electron microscopy (SEM), and catalyst properties, such as; temperature profile of catalyst reduction, metal dispersion, and surface area, were also characterized by $H_2-TPR$ and $H_2-TPD$ techniques, and BET, respectively. From the results, it was found that metal-particle dispersion was relatively high about 5.89%, whereas the surface area of ceramic foam catalysts was $64.52m^2/g$. Finally, the catalytic behaviour toward hydrogen production through the dry reforming of methane using a fixed-bed reactor was evaluated under certain operating conditions. The approaches from this research provide a direction for further improvement of marketable environmental friendly catalyst production.

• Korean Chemical Engineering Research
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• 제56권2호
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• pp.281-290
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• 2018

최근 선진국을 중심으로 고연비-저배출 내연기관 (디젤) 자동차 보급의 필요성이 대두되면서 기존 촉매후처리 장치의 저온성능 강화를 위한 기술적 방안들이 시급히 요구되고 있다. 본 논문에서는 디젤엔진 배출 탄소입자상 물질의 연소반응에 있어 연료함유 촉매(Fuel-Borne Catalyst)와 페로브스카이트(Perovskite)의 복합촉매 시스템이 보이는 상용모델촉매 대비 우수한 저온 연소성능과 이의 Perovskite 촉매 조성에 대한 의존성에 관해 논하였다. Fe/Ce 계열 연료함유 촉매가 A-site 원소(La)에 K이 부분치환되고, B-site 금속이 Fe인 Perovskite 촉매와 복합화될 때 상대적으로 우수한 저온 연소성능 개선효과가 관찰되었다. 이를 관찰하기 위해 연료함유 촉매가 함유되거나 함유하지 않은 탄소 입자상 물질과 다양한 조성의 La 계열 Perovskite 촉매를 혼합한 고정층에 대한 온도상승 산화반응 실험(Temperature-Programmed Oxidation)을 수행하였으며, 이산화탄소 생성과 질소산화물 농도 저하 패턴의 연동특성을 통해 두 촉매의 상호 연계작용을 유추하였다.

• 공업화학
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• 제29권1호
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• pp.103-111
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• 2018

본 연구에서는 온도가 큰 폭으로 변화하는 배기가스에 대응하기 위하여 플라즈마 촉매 공정을 이용하여 넓은 온도범위($150{\sim}500^{\circ}C$)에서 질소산화물($NO_x$)의 전환효율을 향상시키고자 하였다. 촉매 자체의 활성이 높은 고온에서는 $NO_x$저감이 효과적으로 일어나므로 고온 영역에서는 플라즈마 발생을 중지한 채 운전하고, 저온영역에서는 촉매상에 플라즈마를 발생시켜 $NO_x$ 전환효율을 증가시켰다. 촉매의 종류, 반응온도, 환원제(n-헵테인)의 농도 및 에너지 밀도의 변화가 $NO_x$ 전환효율에 미치는 영향을 조사하였다. 다양한 촉매를 비교분석한 결과, 고온에서 촉매에 의한 $NO_x$ 전환효율은 $Ag-Zn/{\gamma}-Al_2O_3$ 촉매의 경우가 90% 이상으로 가장 우수하였다. 저온 영역에서는 탄화수소 선택적 환원 공정에 의해 $NO_x$가 거의 제거되지 않았으나, 플라즈마를 촉매상에서 발생시킬 경우 약 90%의 높은 $NO_x$ 전환효율을 나타내었다. 배기가스의 온도변화에 대응하여 플라즈마를 촉매상에 생성시켜 운전할 경우 $150{\sim}500^{\circ}C$에서 $NO_x$ 전환효율을 높게 유지할 수 있다.

• 한국추진공학회:학술대회논문집
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• 한국추진공학회 2008년도 제30회 춘계학술대회논문집
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• pp.111-114
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• 2008

본 연구에서는 과산화수소 분해 반응을 이용한 초소형 추력기 성능평가를 실시하였다. 물리 화학적 안정성이 뛰어나고 분해 성능이 좋은 백금을 촉매로 사용하고 세라믹 폼을 지지체로 선정하였다. 실험에 사용된 단일 추진제는 90wt% 과산화수소로 질소 가스를 통한 직접 가압 방식으로 추력기에 공급된다. 추력기의 성능을 평가하기 위해서 특성 속도 효율을 구하고 압력곡선을 통해서 압력 상승 시간, 압력 하강 시간, 반응 지연 등을 종합적으로 살펴본다.

• 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.

• 대한기계학회논문집A
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• 제33권3호
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• pp.237-242
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• 2009

MEMS catalytic combustors were fabricated to use in micro-power sources as a heat source. The combustor was fabricated by photolithography and anisotropic wet etching of photosensitive glass wafers. Two different catalyst loading methods were used to complete the fabrication of the combustors. For thin film type, the $Al_2O_3$ was washcoated on the surface of the combustion chamber as a catalyst support, and for packed-bed type, ceramic foam was inserted after Pt was coated. The volume of the combustors was 1.8 $cm^3$ and 16W of heat was generated using the fabricated combustors with hydrogen. The energy density of combustor was about 8.9 W/$cm^3$.

• 한국자동차공학회논문집
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• 제10권2호
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• pp.40-47
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• 2002

Because UV wavelength lights can activate photocatalysts, plasma is used as a light source of a photocatalytic reactor. Even though plasma has good intensity for photo reaction, substrate of catalyst coating was limited by the geometry of plasma generator. Usually bead type substrate was used for a pack bed type reactor. Honeycomb monolith type substrate was used with UV lamps instead plasma, due to the light penetration the honeycomb monolith length was too short to show good activity In this study a photocatalytic reactor, which is using a honeycomb monolith substrate, was investigated with plasma as an activation light source. As a parametric study the effects of 1311owing factors on plasma generation and power consumption are examined; supply voltage, substrate length, environment condition, catalyst loading and ratio. Using the test results, the practicability test was done with simulated synthetic gases representing bad smells and automotive exhaust gases.

• 한국전기화학회:학술대회논문집
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• 한국전기화학회 2003년도 연료전지심포지움 2003논문집
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• pp.89-95
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• 2003

Fuel processing is an enabling technology for faster commercialization under lack of hydrogen infrastructures. It has been reported that the development of novel catalysts that are active and selective for hydrocarbon reforming reactions. It has been realized, however, that with pellet or conventional honeycomb catalysts, the reforming process is mass transport limited. This paper reports the development of catalyst structures with microchannels that are able to reduce the diffusion resistance and thereby achieve the same production rate within a smaller reactor bed. These microchannel reforming catalysts were prepared and tested with natural gas and gasoline-type fuels in a microreactor (1-cm dia.) at space velocities of up to 250,000 per hour. These catalysts have also been used in engineering-scale reactors (10 kWe, 7-cm dia.) with similar product qualities. Compared to pellet catalysts. the microchannel catalysts enable a nearly 5-fold reduction in catalyst weight and volume.