• Applied Chemistry for Engineering
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• v.32 no.6
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• pp.695-699
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• 2021

In this study, Selective Catalytic Reduction on Diesel Particulate Filter (SDPF) after-treatment system was introduced to simultaneously remove NO_x and Particulate Matters (PM) emitted from trucks and special cargo vehicles using old engine. First, in order to select an Selective Catalytic Reduction (SCR) catalyst for SDPF, the de-NO_x performance of V/TiO₂ and Cu-Zeolite catalysts were compared, and the SCR catalyst characteristics were analyzed through Brunauer Emmett Teller (BET), X-ray Diffraction (XRD) and NH3-TPD (Temperature Programmed Desorption). From the activity test results, the Cu-zeolite catalyst showed the best thermal stability. For optimal coating of SDPF, slurry was prepared according to the target particle size. From the coating stability and back pressure test results of SDPF according to the amount of SCR coating, As a result of comparing coating stability, back pressure, and de-NOx performance by producing A, B, and C samples for each loading amount of the SDPF catalyst, the best results were found in the B sample. The engine dynamometer test was conducted for the optimal SDPF after-treatment system, and the test results satisfied Eu-5 regulations.

• Korean Chemical Engineering Research
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• v.48 no.1
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• pp.10-15
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• 2010

Intensive works have been carried out to develop more efficient solid catalysts for biodiesel production from various feedstocks including refined oils and waste fats. Among many catalysts, metal oxides and ion exchange resins are the most intensively studied ones. With regard to metal oxide catalysts, major research activities have focused on the identification of the active compounds and their immobilizing methods on the supports. As metal oxide catalysts have strong thermal stability, they may be used in simultaneous transesterification and esterification of waste fats. However, ion exchange resin catalysts were mainly applied in the esterification of the free fatty acids in waste fats because of their lower thermal stability. For both solid catalysts, further works are needed to make them to be used in commercial process. Especially fast deactivation of the solid catalyst would be the most challenging problem.

• The Microorganisms and Industry
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• v.20 no.1
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• pp.38-41
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• 1994

아미노산은 발효법, 합성법, 효소법, 추출법 등으로 제조되고 있으며, 아미노산 시장의 대부분을 차지하는 glutamic acid, lysine, methionine, glycine, phenylalanine등의 주요 아미노산은 전통적인 발효법과 합성법에 의해 주로 제조되고 있다(1-3). 표 1에 주요 아미노산의 생산량, 제조법, 용도들을 표시하였다. 최근 고정화효소법 및 화학합성법과 효소법을 병행한 반합성법(hybrid process 또는 chemico-enzymatic process라고도 함) 등의 새로운 아미노산 제조법(3-7)이 개발되어 주목되고 있다. 이러한 새로운 아미노산 제조법은 효소를 촉매라는 시각에서 수행하고 있기 때문에 생물촉매법이라 총칭하며, 생물촉매법은 화학반응으로는 곤란한 반응을 효소반응의 도입에 의하여 효율적으로 수행할 수 있는 특징과 각종 연관 아미노산 화합물을 동시에 제조할 수 있다는 대단히 유리한 장점 때문에 새로운 아미노산 제조법으로 점차 기업화되고 잇는 추세이다. 따라서, 본고에서는 생물촉매를 이용한 아미노산의 새로운 제조법에 대하여 소개하고자 한다.

• Journal of the Korean Applied Science and Technology
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• v.35 no.1
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• pp.151-156
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• 2018

As industry and medicine developed, many people became interested in the quality of life. As the concern for health became higher, vegetarian or vegetable oils became more popular than meat. With the development of processes primarily using nickel catalysts today, the shelf life of vegetable oils has increased and mobility has become more convenient. Currently nickel catalysts for the curing of oil are dominated by foreign companies in the world market. On the other hand, the mass production technology of domestic nickel catalyst is backward, and the entire amount is imported from foreign countries. Therefore, there is a need for active research and development of a catalyst that can be commercialized in korea. In this study, nickel as a main active catalyst was used as a base for hydrogen curing reaction, and the effect of rare earth on catalytic activity was investigated. A certain amount of rare earths could induce the dispersion of nickel to increase efficiency and use as co-catalyst.

• Clean Technology
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• v.15 no.1
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• pp.42-46
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• 2009

Solvent-free direct preparation of dichloropropanol (DCP) from glycerol (by-product of bio-diesel production) and hydrochloric acid gas was carried out over acetin catalyst in a gas-liquid batch reactor. For this purpose, acetin mixture and triacetin were used as a homogeneous acetin catalyst. Performance in the acetin-catalyzed reaction was compared to that in the non-catalytic reaction under the same reaction conditions ($110^{\circ}C$, 3 bar, 3 h). Conversion of glycerol in the acetin-catalyzed reactions was ca. 3% higher than that in the non-catalytic reaction, and selectivity for dichloropropanol in the acetin-catalyzed reactions was ca. 50% higher than that in the non-catalytic reaction. It was also revealed that the catalytic performance of triacetin was ca. 2% higher than that of acetic mixture.

• Journal of Energy Engineering
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• v.17 no.2
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• pp.100-106
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• 2008

Flameless fiber mat catalytic burners have been known as an effective heat source in industrial drying processes since heat obtained from combustion can be transferred to absorptive body by far-infrared radiation. In order to extend the application of fiber mat catalytic burner, novel fiber mat catalytic burners were manufactured and combustion characteristics of them were investigated. For diffusive catalytic burners, the efficiency of combustion was significantly affected by the installation direction and the temperature of catalytic bed perimeter influenced on the diffusion rate of oxygen which determined the combustion efficiency of catalytic burner. It was seen in premixed catalytic combustion that air content in premixed fuel gas was optimized at slightly higher than theoretical amount of air. Combustion heat released higher than 70% by radiant heat in premixed catalytic combustion likewise diffusive catalytic combustion.

• Aerospace Engineering and Technology
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• v.4 no.1
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• pp.49-56
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• 2005

Hot firing performance test of hydrazine decomposition catalyst used for monopropellant thruster of the satellite and the launch vehicle was performed. Test equipment for catalyst test was developed in collaboration with Hanwha Corp., reaction delay time, catalyst activity and granule stability of the catalyst firing performance were measured and analyzed with the equipment. In addition, the current development of prototype catalyst is introduced.

• Proceeding of EDISON Challenge
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• 2016.03a
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• pp.330-332
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• 2016

수소 발생 반응 촉매는 주로 백금(Pt)족 물질로 만들어져왔으나, 그 높은 가격과 희귀성으로 인해 이를 대체할 촉매의 개발이 요구되고 있다. 그중에서 주목받는 물질이 판상 $MoS_2$인데, 순물질로써의 $MoS_2$는 오직 모서리 부분만이 촉매로 기능하며 표면은 안정하여 촉매로써 기능을 하지 못한다는 한계가 있었다. 따라서 $MoS_2$의 표면도 촉매로 기능하여 보다 효율적인 촉매가 될 수 있도록, 자연계에 비교적 풍부한 원소들로 Mo원자를 치환해 보고 평면 스트레인을 줌으로써 표면이 촉매로 기능할 수 있는 조건을 밀도 범함수 이론에 근거해 계산해 보았다. 그 결과, Ge로 치환되고 -10% 스트레인이 걸린 $MoS_2$의 표면이 촉매로 기능할 수 있는 조건을 만족시켰다. 한편 Ge로 치환된 샘플에 수소를 흡착시켰을 때, 치환된 원자와 수소 원자가 반발력을 나타내는 듯한 현상이 관찰되었다.

• Applied Chemistry for Engineering
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• v.10 no.2
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• pp.263-267
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• 1999

NO removal activity (per unit of mass) of the used catalyst was seriously decreased as low as 27% of the new catalyst. Since the surface area of the used catalyst was 63% of that of the new one, the mojor reason for the lessened activity of the used catalyst compared to the new one may be due to the decreased surface area by sintering and surface concentration of active materials. Poison may be regarded as another important factor, since it affect the active site of catalyst by heavy metals. To recycle the used catalyst, we focused on the removal of poisoning agents from the catalyst. By using $80^{\circ}C$ water for 30 min upto 2 h, the recycled catalyst demonstrated the best activity and efficiency, which may be due to the removal of both K and Na. Although the recovered activity (per unit of surface area) of the catalyst was 79% compared to the new one, the activity (per unit of mass) of the recovered catalyst was only 49% compared of the activity of fresh catalyst.

• 한국신재생에너지학회:학술대회논문집
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• 2011.05a
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• pp.177.1-177.1
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• 2011

국내 바이오디젤의 원료로 사용되는 식물성 오일은 거의 전량이 수입된 것으로 원료를 자급화 하기 위한 방안으로 국내 동물성 폐자원을 이용한 바이오디젤 연구가 활발히 진행되고 있다. 본 연구에서는 전자레인지를 이용해 동물성 폐자원인 폐돈지 및 폐우지로부터 오일을 추출 후 물성을 분석하고 전이에스테르화 반응을 진행하였으며 바이오디젤 제조 특성을 조사하고자 하였다. 전이에스테르화 반응에 사용되는 염기 촉매를 몇가지 선정하여 각각의 촉매에 따른 바이오디젤의 반응특성을 메탄올 양을 변화시키며 조사 실험하였다. 기존에 사용된 바이오디젤 제조 촉매는 KOH를 주로 사용하였으며 본 연구에서는 KOH, NaOH, $NaOCH_3$를 촉매로 사용하여 오일질량 대비 0.8~1.2%의 촉매를 사용하였으며 메탄올의 양은 오일 몰수 대비 6:1~12:1의 비율로 사용하여 반응시간에 따른 반응특성과 제조 바이오디젤의 물성을 분석해 각 촉매에 따른 바이오디젤 생산 특성을 비교분석하였다.