发明名称 DUAL CATALYST BED REACTOR FOR METHANOL OXIDATION
摘要 A process and apparatus for oxidizing methanol in a gas stream formaldehyde in a fixed bed reactor. The process first introduces a gas stream into a fixed bed reactor. The fixed bed reactor contains a catalyst bed having a depth, a width, a length, an inlet, an upstream region, a downstream region and an outlet. Preferably, the inlet, the upstream region, the downstream region and the outlet are provided in the order stated. A vanadia-titania catalyst is provided in the upstream region and a molybdena-titania catalyst is provided in the downstream region.The vanadia-titania catalyst in the upstream region is substantially free of MoO3 and initially (i.e., during oxidation some V2O5 may sublime and migrate to the downstream region) the molybdenatitania catalyst in the downstream region is substantially free V2O5. Next, the gas stream is contacted with a vanadia-titania catalyst under oxidizing conditions. Then, the gas stream is contacted with a molybdnea-titania catalyst under oxidizing conditions which provides a product stream containing formaldehyde at the desired conversion and formaldehyde selectivity.
申请公布号 WO0222540(A3) 申请公布日期 2002.08.15
申请号 WO2001US28353 申请日期 2001.09.13
申请人 LEHIGH UNIVERSITY 发明人 WACHS, ISRAEL, E.
分类号 B01J23/22;B01J23/28;B01J35/00;C07C45/38;C07C47/052 主分类号 B01J23/22
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