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Recovery of Useful Hydrocarbons from Petroleum Residual Oil by Catalytic Cracking with Steam over Zirconia-Supporting Iron Oxide Catalyst
To reduce the consumption of hydrogen when converting heavy oil to light oil, the catalytic cracking of a heavy oil (residue of atmospheric distillation) with steam was examined. Two iron oxide-based catalystshematite (α-Fe2O3) and goethite (FeOOH, denoted herein as FeO X catalyst)were used. It wa...
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Published in: | Energy & fuels 2004-11, Vol.18 (6), p.1770-1774 |
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Main Authors: | , , , |
Format: | Article |
Language: | English |
Subjects: | |
Citations: | Items that this one cites Items that cite this one |
Online Access: | Get full text |
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Summary: | To reduce the consumption of hydrogen when converting heavy oil to light oil, the catalytic cracking of a heavy oil (residue of atmospheric distillation) with steam was examined. Two iron oxide-based catalystshematite (α-Fe2O3) and goethite (FeOOH, denoted herein as FeO X catalyst)were used. It was found that the heavy oil was converted to a mixture of useful light hydrocarbons (i.e., gasoline, kerosene, and gas-oil) over iron oxide-based catalysts. Moreover, because the FeO X catalyst possessed mesopores with diameters of 6−10 nm, it exhibited higher activity than the α-Fe2O3 catalyst without the production of carbonaceous residue. The catalytic activity could be enhanced by loading ZrO2 on the FeO X catalyst. From the X-ray diffraction analysis and Mössbauer measurement, it was considered that the active oxygen species generated from H2O over ZrO2 particles spilled over the FeO X surface, where the oxidized decomposition of heavy oil occurred. |
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ISSN: | 0887-0624 1520-5029 |
DOI: | 10.1021/ef0499067 |