Journal of the Korean Industrial and Engineering Chemistry, Vol.11, No.8, 903-909, December, 2000
TiO2(anatase)에 담지된 Vanadium-Phosphorus 산화물 촉매상에서 시클로펜텐의 선택적 산화반응
Selective Oxidation of Cyclopentene on TiO2(anatase)-supported Vanadium-Phosphorus Oxide Catalysts
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초록
V-P(vanadium-phosphorus)/TiO2(anatase) 촉매들 위에서 무수말레인산(MA) 및 무수프탈산(PA)으로의 시클로펜텐 선택적 산화반응을 연구하였다. 3.5 wt%의 담지량을 가진 촉매들에서 V-P 활성 성분들은 얇은 층으로서 작은 표면적의 TiO2(anatase) 표면위에 잘 분산되었으며, 적절한 P/V 원자비를 가진 촉매들은 시클로펜텐의 선택적 산화를 위하여 효과적인 것으로 발견되었다. 이 촉매들에서, P(phosphorus)함량이 증가됨에 따라 산화 활성은 감소되었다. MA로의 선택성은 P 함량 증가에 따라 증가하다가 0.5의 P/V 원자비에서 최고값을 나타낸 후 감소되었으며, PA로의 선택성은 연구된 0∼1.1의 P/V 원자비 범위에서 점차적으로 증가하였다. 원하는 생성물들인 MA와 PA로의 선택성들의 합에 의해 결정된 최고값은 약 50%로서 0.7의 P/V원자비를 가진 촉매에서 나타났다. 다른 한편, 0.7의 P/V 원자비에서 담지량의 증가는 산화 활성과 원하는 생성물들로의 선택성에서의 미시적인 감소를 결화했다. 이에 더하여, P/V 원자비에 기인한 효과들이 시클로펜텐의 선택적 산화반응을 위한 반응 메카니즘과 연결하여 논의하였다.
The selective oxidation of cyclopentene to maleic anhydride (MA) and phthalic anhydride (PA) has been studied using V-P(vanadium-phosphorus) oxide catalysts supported by TiO2(anatase). In the catalysts with 3.5 wt% V-P loading, V-P active components were effectively dispersed on a low surface area of TiO2(anatase) forming thin layers. The catalysts with appropriate P/V ratios were effective in the selective oxidation of cyclopentene. As the content of P (phosphorus) in the active component of the catalysts was increased, the oxidation activity was decreased, but the selectivity of MA was increased to a maximum at the P/V atomic ratio of 0.5 before decrease. For P/V atomic ratios of 0∼1.1, however, the selectivity of PA was gradually increased. A maximum value determined by the sum of the selectivities of MA and PA, was obtained at the P/V atomic ratio of 0.7 and ca.(????) 50%. On the other hand, the increased loading of active components in the P/V atomic ratio of 0.7 resulted in minor decreases of the oxidation activity and the selectivity of the desired products, MA and PA. In addition, the effects due to P/V atomic ratios were discussed in connection with the reaction mechanism for the selective oxidation of cyclopentene.
- Schleppinghoff B, Schulwitz B, Erdol Kohle Erdgas Petrochem., 38, 209 (1985)
- Griesbaum K, Honicke D, "Ullmanns Encyclopedia of Industrial Chemistry," 5th ed., A8, 227, VCH Verlagsgesellschaft, Heidelberg (1987)
- Bockler R, Cordes G, Smolen H, Chem. Ing. Tech., 62, 447 (1990)
- Griesbaum K, Honicke D, Erdol Kohle Erdgas Petrochem., 35, 102 (1986)
- Yang HS, Kim YH, J. Korean Ind. Eng. Chem., 7(5), 888 (1996)
- Kim YH, Yang HS, Korean J. Chem. Eng., 17(3), 357 (2000)
- Bond GC, Tahir SF, Appl. Catal., 71, 1 (1991)
- Bond GC, "Handbook of Heterogeneous Catalysis," Vol. 2, ed. by G. Ertl, H. Knozinger and J. Weitkamp, 752, VCH, Weinheim (1997)
- Saleh RY, Wachs IE, Appl. Catal., 31, 87 (1987)
- Nikolov V, Klissurski D, Anastasov A, Catal. Rev.-Sci. Eng., 33, 319 (1991)
- Dias CR, Portela MF, Catal. Rev.-Sci. Eng., 39(3), 169 (1997)
- Centi G, Burattini M, Trifiro F, Appl. Catal., 32, 353 (1987)
- Centi G, Trifiro F, Catal. Today, 3, 151 (1988)
- Centi G, Nieto JL, Pinelli D, Trifiro F, Ind. Eng. Chem. Res., 28, 400 (1989)
- Busca G, Centi G, J. Am. Chem. Soc., 111, 46 (1989)
- Centi G, Trifiro F, Chem. Eng. Sci., 45, 2589 (1990)
- Bond G, Bosch H, Ommen JGV, Kip BJ, Appl. Catal., 22, 361 (1986)
- Roozeboom F, Mittelneijer-Hazeleger MC, Moulijn JA, Medema J, de Beer VHJ, Gellings PJ, J. Phys. Chem., 84, 2783 (1980)
- Dias CR, Portela MF, Bond GC, J. Catal., 157(2), 344 (1995)
- Centi G, Nieto JL, Pinelli D, Trifiro F, Ungarelli F, "new Developments in Selective Oxidation" ed. by G. Centi and F. Trifiro, 635, Elsevier Science Publishers B.V., Amsterdam (1990)
- Deo G, Wachs IE, J. Catal., 146(2), 335 (1994)