Millisecond Catalytic Reforming of Monoaromatics over Nobel Metals

被引:13
作者
Balonek, C. M. [1 ]
Colby, J. L. [1 ]
Schmidt, L. D. [1 ]
机构
[1] Univ Minnesota, Dept Chem Engn & Mat Sci, Minneapolis, MN 55455 USA
基金
美国国家科学基金会;
关键词
reactor; catalysis; autothermal; monoaromatic; benzene; toluene; ethylbenzene; cumene; styrene; rhodium; SHORT-CONTACT TIMES; PARTIAL OXIDATION; FLUIDIZED-BED; BENZENE; PYROLYSIS; TOLUENE; HYDROCARBONS; BIOMASS; ETHYLBENZENE; POLYSTYRENE;
D O I
10.1002/aic.12045
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The millisecond autothermal reforming of benzene, toluene, ethylbenzene, cumene, and styrene were independently studied over,five noble metal-based catalysts: Pt, Rh, Rh/gamma-Al2O3, Rh-Ce, and Rh-Ce/gamma-Al2O3, as a function of carbon-to-oxygen feed ratio. The Rh-Ce/gamma-Al2O3 catalyst exhibited the highest feedstock conversion as well as selectivities to both synthesis gas and hydrocarbon products (lowest selectivities to H2O and CO2). Experimental results demonstrate a high stability of aromatic rings within the reactor system. Benzene and toluene seem to react primarily heterogeneously, producing only syngas and combustion products. Ethylbenzene and cumene behaved similarly, with higher conversions than benzene and toluene, and high product selectivity to styrene, likely due to homogeneous reactions involving their alkyl groups. Styrene exhibited low conversions over Rh-Ce/gamma-Al2O3, emphasizing the stability of styrene in the reactor system. (C) 2009 American Institute of Chemical Engineers AIChE. J, 56: 979-988. 2010
引用
收藏
页码:979 / 988
页数:10
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