• Title/Summary/Keyword: Zeolite catalyst

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Micro Gas Turbine Performance using Catalytic Cracked Ethanol as Fuel (촉매 분해 에탄올을 연료로 사용하는 마이크로 가스터빈의 성능)

  • Choi, Songyi;Koo, Jaye;Yoon, Youngbin
    • Journal of Aerospace System Engineering
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    • v.11 no.2
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    • pp.9-15
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    • 2017
  • In order to verify the possiblity of improving the combustion performance of ethanol using zeolite catalyst and the characteristics of nitrogen oxides and carbon monoxide emission, micro gas turbine experiments were performed using catalytic reaction products, ethanol and kerosene as fuels and the results were compared. The thrust of the catalytic reaction product was lower than that of kerosene, but it was improved by 5% on average compared with the use of ethanol. Nitrogen oxides and carbon monoxide emissions of the catalytic reaction products were measured to be very low overall compared to kerosene. As a result, when the ethanol was reformed using the zeolite catalyst, the engine performance could be improved while maintaining the environment friendliness of the ethanol.

Catalytic Technology for NOx Abatement using Ammonia (암모니아를 환원제로 이용한 NOx 저감 촉매 기술)

  • Park, Soon Hee;Lee, Kwan-Young;Cho, Sung June
    • Clean Technology
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    • v.22 no.4
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    • pp.211-224
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    • 2016
  • Three way catalyst has been used extensively for the exhaust gas treatment for the internal combustion gasoline engine. While, numerous research efforts have been directed to develop various technologies for the abatement of exhaust gas from diesel engine. Diesel engine operating under lean condition produces large amount of NOx and the corresponding catalytic technology employing vanadium supported titania using ammonia has been commercialized for heavy duty vehicle. Recently, the Cu catalyst supported on zeolite has been investigated for NOx abatement using ammonia because of its critical importance for ultra low emission vehicle. The current review shows the recent trend in research and development for zeolite based copper catalysts, which are mainly used as catalysts for selective catalytic reduction using ammonia, are one of the aftertreatment technologies for effectively removing nitrogen oxides from diesel exhaust.

A Study of Pt-Mg/Mesoporous Aluminosilicate Catalysts for Synthesis of Jet-fuel from n-Octadecane (n-Octadecane 으로부터 항공유 제조를 위한 Pt-Mg/mesoporous aluminosilicate 촉매 연구)

  • Jung, Euna;Kim, Chul-Ung;Jeon, Jong-Ki
    • Korean Chemical Engineering Research
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    • v.54 no.5
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    • pp.712-718
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    • 2016
  • Platinum catalysts supported on the mesoporous material synthesized from Y zeolite were applied to synthesis of jet-fuel through n-octadecane hydroupgrading. The mesoporous aluminosolicate, $MMZ_{HY}$ was synthesized using Y zeolite as its framework source. The effect of the addition of Mg to $Pt/MMZ_{HY}$ catalyst for n-octadecane hydroupgrading was investigated. Catalyst characterization was performed with X-ray diffraction, $N_2$ adsorption, temperature-programmed reduction in hydrogen flow, temperature-programmed desorption of ammonia, and infrared spectroscopy of adsorbed pyridine. The high yield of jet-fuel over the $PtMg(2.0)/MMZ_{HY}$ can be attributed not only to the higher dispersion of Pt metal and higher reducibility, but also the higher amount of acid sites and higher strength of acid sites. The selectivity to iso-paraffin in the jet-fuel fraction could be reached above 80% over the optimized $PtMg/MMZ_{HY}$ catalyst.

The Study of Toluene Combustion over Palladium-copper/USY Zeolite Catalyst (Pd-Cu/USY 제올라이트상에서 톨루엔 연소반응 연구)

  • Lee, Hye Young;Jin, Taihuan;Hwang, Young Kyu;Chang, Jong-San;Hwang, Jin-Soo;Lee, Chang-Gook;Baek, Shin;Ra, Do-Young
    • Korean Chemical Engineering Research
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    • v.44 no.4
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    • pp.404-409
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    • 2006
  • The catalytic combustion of toluene over Pd-Cu/USY zeolite has been examined by using FT-IR spectroscopy in a closed system under dry and humid conditions. The catalytic combustion of toluene (700 ppmv) in the temperature range of $80-220^{\circ}C$ has been investigated by using a fixed bed reactor. The Pd-Cu/USY catalyst showed the highest catalytic performance with respects to the PdO-CuO/USY and Pd/USY. Comparing to $PdO/Al_2O_3$ catalysts, the slight improvement in conversion was observed over PdO/USY catalysts under humid condition since USY zeolite is hydrophobic substrate and water give an additional oxygen source to zeolite surface like oxygen. The reduced catalysts showed more enhanced catalytic activity due to the reduced activation energy of combustion of toluene than oxidized catalysts such as PdO/USY and PdO-CuO/USY.

Synthesis of Conjugated Linoleic Acid Methylester using Heterogeneous Catalysts (불균일계 촉매에 의한 공액 리놀레산 메틸에스테르의 합성)

  • Yuk, Jeong-Suk;Lee, Sang-Jun;Kim, Nam-Kyun;Kim, Young-Wun;Yoon, Byeong-Tae
    • Applied Chemistry for Engineering
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    • v.24 no.3
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    • pp.291-298
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    • 2013
  • Conjugated linoleic acid methylester was synthesized through isomerization of linoleic acid methylester by using heterogeneous catalysts. As for heterogeneous catalysts, Ni supported zeolite type catalysts were used. H zoelite Y (HY) were ion exchanged with KCl aqueous solution to synthesize K zeolite Y (KY), and with impregnation method, Ni supported zeolite catalysts were synthesized. Catalysts were used after pre-treatment by using hydrogen. HY catalysts showed a high conversion at low temperatures; but a low selectivity for conjugation reaction. KY catalysts showed a low conversion at low temperatures; but a similar conversion with HY catalysts at high temperatures while a high selectivity at low temperatures. As a result, 4 wt% Ni/KY720 recorded the high conjugation yield of 63.4% at 220.

Effect of Different Zeolite Supported Bifunctional Catalysts for Hydrodeoxygenation of Waste Wood Bio-oil

  • Oh, Shinyoung;Ahn, Sye-Hee;Choi, Joon Weon
    • Journal of the Korean Wood Science and Technology
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    • v.47 no.3
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    • pp.344-359
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    • 2019
  • Effects of various types of zeolite on the catalytic performance of hydrodeoxygenation (HDO) of bio-oil obtained from waste larch wood pyrolysis were investigated herein. Bifunctional catalysts were prepared via wet impregnation. The catalysts were characterized through XRD, BET, and SEM. Experimental results demonstrated that HDO enhanced the fuel properties of waste wood bio-oil, such as higher heating values (HHV) (20.4-28.3 MJ/kg) than bio-oil (13.7 MJ/kg). Water content (from 19.3 in bio-oil to 3.1-16.6 wt% in heavy oils), the total acid number (from 150 in bio-oil to 28-77 mg KOH/g oil in heavy oils), and viscosity (from 103 in bio-oil to $40-69mm^2/s$ in heavy oils) also improved post HDO. In our experiments, depending on the zeolite support, NiFe/HBeta exhibited a high Si/Al ratio of 38 with a high specific surface area ($545.1m^2/g$), and, based on the yield of heavy oil (18.3-18.9 wt%) and HHV (22.4-25.2 MJ/kg), its performance was not significantly affected by temperature and solvent concentration variations. In contrast, NiFe/zeolite Y, which had a low Si/Al ratio of 5.2, exhibited the highest improved quality for heavy oil at high temperature, with an HHV of 28.3 MJ/kg at $350^{\circ}C$ with 25 wt% of solvent.

Preparation of Alumino-silicate Membrane and Its Application to a Gas Separation

  • 김태환
    • Proceedings of the Membrane Society of Korea Conference
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    • 2002.04a
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    • pp.23-46
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    • 2002
  • The cryogenic, pressure swing adsorption and membrane methods have been used to separate air into nitrogen and oxygen. The air separation membrane is made of the polymers, of which manufacturing process is complicate and it causes a little high production cost. Polymer membrane has temperature limit in usage and low durability even at moderate temperature. Therefore, inorganic membranes have been studied for years. As formation of unit alumino-silicate membrane, unit cells of membrane were made with a few coating methods. In this study the dipping of substrate into sols, application of vacuum to the opposite side of substrate with coating and rotating of the substrate in the sols were found as good coating memthods to make a uniform coating and to control the thickness of membrane. The membrane coats were examined by SEM and XRD. The sample ESZl-1 was compared with those of samples that prepared by another method. The present developed coating methods could be applied to the various types of zeolite membrane formation, that is A- X-, Y- ZSM- and MCM-types of membranes. Also these membrane forming methods could be applied to formation of catalyst absorbed zeolite membrane, of which zeolite absorb the catalytic metals. The product obtained from these coating methods could be applied to the industrial gas and liquid phase catalytic reaction and separation processes.

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Characterization of NaX zeolite catalyst as the amount of KOH for the Biodiesel Production (NaX 제올라이트 촉매에 담지된 KOH의 양에 따른 바이오디젤 합성 특성)

  • Kim, Jang-Mi;Kim, Min-Kyu;Chang, Duk-Rye
    • 한국신재생에너지학회:학술대회논문집
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    • 2009.11a
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    • pp.521-523
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    • 2009
  • 본 연구에서는 식물성유지와 메탄올로부터 전이에스테르화 반응에 의해 바이오디젤 제조에 사용되는 비균질촉매로 사용하기 위하여 NaX 제올라이트 촉매에 염기도를 향상시키기 위하여 KOH를 담지하여 담지량에 따른 바이오디젤 제조특성을 조사해보았다. KOH 담지량을 10wt% - 70wt%로 달리하여 Incipient wetness 방법으로 담지한후 $500^{\circ}C$에서 소성하여 촉매를 제조하고, 제조된 KOH의 담지량이 다른 KOH/NaX 제올라이트 촉매는 SEM, XRD, BET등을 통해 촉매특성을 평가하였고, 생성된 지방산 메틸에스테르는 가스크로마토그래피로 순도를 측정하였다. NaX 제올라이트 촉매에 KOH 담지량이 높은 경우와 촉매량이 많은 경우 바이오디젤제조에 유리하였고, 특히 반응시간과 반응온도는 $120^{\circ}C$, 2시간동안 반응한 경우 가장 좋은 지방산 메틸에스테르의 수율을 얻을 수 있었다.

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Characterization of NaX zeolite catalyst as the amount of KOH for the Biodiesel Production (NaX 제올라이트 촉매에서 KOH 담지량에 따른 바이오디젤 합성 특성)

  • Chang, Duk-Rye;Kim, Jin-Hyeok
    • 한국신재생에너지학회:학술대회논문집
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    • 2008.10a
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    • pp.83-84
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    • 2008
  • 바이오 디젤은 석유기반 연료들을 대신할 수 있는 대체연료일 뿐만 아니라 재생가능자원으로부터 얻을 수 있다는 장점을 가지고 있다. 바이오 디젤은 동 식물성 유지를 이용해서 알코올과 촉매 존재하에서 제조되며, 주로 KOH, NaOH 등 균질촉매를 이용하여 제조하는데 이는 폐수 발생이 많고 공정 비용이 많이 든다는 단점이 있다. 따라서 최근에는 폐기물 발생이 없고 촉매의 제거가 편리한 비균질촉매의 개발이 이루어지고 있다. 본 연구에서는 NaX 제올라이트 촉매에 KOH를 담지시켜 염기도의 증가에 따라 바이오디젤의 제조특성에 미치는 촉매특성을 조사해 보았다. NaX 제올라이트 촉매에 KOH 담지량이 증가와 반응시간이 증가함에 따라 바이오디젤 생성량은 증가하였다.

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The $CO_{2}$ Hydrogenation toward the Mixture of Methanol and Dimethyl Ether: Investigation of Hybrid Catalysts

  • 준기원;K.S. Rama Rao;정미희;이규완
    • Bulletin of the Korean Chemical Society
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    • v.19 no.4
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    • pp.466-470
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    • 1998
  • Catalytic hydrogenation of carbon dioxide for the simultaneous synthesis of methanol and dimethyl ether (together called oxygenates) over a combination of methanol synthesis and methanol dehydration catalysts has been studied. Various methanol synthesis and methanol dehydration catalysts were examined for this reaction. The addition of promotors like $Ga_2O_3\; and\; Cr_2O_3$ to Cu/ZnO catalyst gave much more enhanced yield on the formation of oxygenates. From the results, the promotional effect of $Cr_2O_3$ has been explained in terms of increase in the intrinsic activity of Cu while that of $Ga_2O_3$ being increase in the dispersion of Cu. Among the methanol dehydration catalysts examined, the solid acids bearing high population of intermediate-strength acid sites were found to be very effective for the production of oxygenates. HY zeolite which contains strong acid sites produce small amount of hydrocarbons as by-products. However, CuNaY zeolite in which the presence of strong acid sites are minimum gives very high oxygenates yield without the formation of hydrocarbons.