• Title/Summary/Keyword: catalytic combustion of benzene

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Catalytic Combustion of Benzene over Metal Ion-Substituted Y-Type Zeolites (금속이온이 치환된 Y형 제올라이트에서 벤젠의 촉매연소반응)

  • Hong, Seong-Soo
    • Clean Technology
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    • v.22 no.3
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    • pp.161-167
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    • 2016
  • Catalytic combustion of benzene over various metal cation-exchanged zeolites has been investigated. Y(4.8)-type zeolite showed the highest activity among the used zeolites and Cu/Y(4.8) catalyst also showed the highest activity among metal cation/ Y(4.8) zeolites. The catalytic activity increased according to the amount of adsorbed oxygen acquired from O2 TPD results. The catalytic activity also increased with an increase of Cu cation concentration on Cu/Y(4.8) catalysts. The conversion of benzene on the combustion reaction depended on not benzene concentration but the oxygen concentration. In addition, the introduction of water into reactants decreased the catalytic activity.

Catalytic Combustion of Benzene over CuO-CeO2 Mixed Oxides Prepared by Co-precipitation Method (침전법으로 제조된 CuO-CeO2 혼합산화물에서 벤젠의 촉매연소반응)

  • Hong, Seong Soo
    • Applied Chemistry for Engineering
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    • v.25 no.3
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    • pp.312-317
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    • 2014
  • Catalytic combustion of benzene over CuO-$CeO_2$ mixed oxides prepared by co-precipitation method were investigated. The CuO-$CeO_2$ mixed oxides were also prepared using different precipitant and CuO precursor. They were characterized by XRD, BET, XPS and $H_2-TPR$. In the CuO-$CeO_2$ catalysts, characteristic copper oxide peaks were shown at $2{\Theta}=35.5^{\circ}$ and $38.5^{\circ}$ regardless of the precipitant. The Cu0.35 catalyst prepared using $NH_4OH$ as a precipitant revealed the highest activity on the combustion of benzene. In addition, the pretreatment with hydrogen enhanced the catalytic activity and the catalyst reduced at $400^{\circ}C$ showed the highest activity on the combustion of benzene.

Catalytic Combustion of Benzene over Perovskite-type Oxides Prepared Using Malic Acid Method (능금산법으로 제조된 페롭스카이트형 산화물에서 벤젠의 촉매연소반응)

  • Jung, Won-Young;Hong, Seong-Soo
    • Clean Technology
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    • v.18 no.3
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    • pp.259-264
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    • 2012
  • Perovskite-type oxides were successfully prepared using malic acid method, characterized by TG/DTA, XRD, XPS, TEM and $H_2$-TPR and their catalytic activities for the combustion of benzene were determined. Almost of catalyst showed perovskite crystalline phase and 15-70 nm particle size. The $LaMnO_3$ catalysts showed the highest activity and the conversion reaches almost 100% at $350^{\circ}C$. The catalysts were modified to enhance the activity through substitution of metal into the A or B site of the perovskite oxides. In the $LaMnO_3$-type catalyst, the partial substitution of Sr into site the A-site enhanced the catalytic activity in the benzene combustion. In addition, the partial substitution of Co or Cu into site the B-site also enhanced the catalytic activity and the catalytic activity was in the order of Co > Cu > Fe in the $LaMn_{1-x}B_xO_3$ (B = Co, Fe, Cu) type catalyst.

Removing Volatile Organic Compound using the Waste Industrial Catalyst - The effect of pretreatment on Pt-based catalyst (폐 산업용 촉매를 이용한 휘발성유기화합물의 제거 -Pt 계 촉매의 전처리 효과-)

  • 김상채;서성규
    • Journal of Korean Society for Atmospheric Environment
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    • v.18 no.3
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    • pp.205-212
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    • 2002
  • The catalytic combustion of benzene, toluene and xylene over Pt-based catalyst was investigated in a fixed bed flow reactor system with atmospheric pressure to recycle the waste industrial catalyst for the processes of removing volatile organic compounds. According to the pretreatment condition, the properties of the waste Pt-based catalyst were characterized by XRD (X-ray diffraction) and BET (Brunauer-Emmett-Toller). In the carte of air pretreatment, 20$0^{\circ}C$ was found to be optimal, and increasing pretreatment temperature resulted in the reduction of the catalytic activity. When Pt-based catalyst pretreated at 20$0^{\circ}C$ by alto was retreated by hydrogen, the catalytic activity increased by increasing treatment temperature. In the case of HNO$_3$aqueous solution pretreatment, the catalytic activity decreased by increasing the concentration of HNO$_3$aqueous solution. The catalytic activity was seen to observe the following sequence : benzene > toluene > xylene.

Combustion Characteristics of Benzene over $LaMnO_3$ Perovskite-type Catalysts Prepared Using Microwave-assisted Process (마이크로파 공정으로 제조된 $LaMnO_3$ 페롭스카이트형 촉매에서 벤젠의 연소반응)

  • Jung, Won Young;Hong, Seong-Soo
    • Applied Chemistry for Engineering
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    • v.24 no.5
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    • pp.507-512
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    • 2013
  • Perovskite-type oxides were successfully prepared using microwave-assisted process, and by XRD, XPS, BET, and $H_2-TPR$. Their catalytic activities for the combustion of benzene were also examined. Most of catalysts studied showed the perovskite crystalline phase with the particle size of 21~35 nm. The $LaMnO_3$ catalyst showed the highest activity and the conversion reached almost 100% at $250^{\circ}C$. The catalysts prepared by microwave-assisted process showed higher activity compared to those prepared sol-gel method. In addition, the catalytic activity was increased with an increase of calcination temperature of $LaMnO_3$-type catalyst. The TPR results on the measurement of redox property showed a good correlation with the order of catalytic activity on the benzene combustion reaction.

Complete Combustion of Benzene over CuO/CeO2 Catalysts Prepared by Various Methods (다양한 방법으로 제조된 CuO/CeO2 촉매에서의 벤젠의 연소반응)

  • Jung, Won Young;Song, Young In;Hong, Seong-Soo
    • Clean Technology
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    • v.19 no.2
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    • pp.128-133
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    • 2013
  • Catalytic combustion of benzene over $CeO_2$-supported copper oxides has been investigated. The supported copper oxides catalysts were prepared using ball mill method and characterized by XRD, FT-IR, TEM and TPR. In the CuO/$CeO_2$ catalysts prepared using ball mill method, highly dispersed copper oxide species were shown at high loading ratio. The CuO/$CeO_2$ prepared using ball mill method showed the higher activity than those prepared using impregnation method. The catalytic activity increased with an increase in the CuO loading ratio, 10 wt% loaded CuO/$CeO_2$ catalyst giving the highest activity. In addition, the promoting of 10 wt% loaded CuO/$CeO_2$ catalyst with $Fe_2O_3$ and CoO enhanced the dispersion of CuO and then increased the catalytic activity.