发明名称 Dehydrocyclization process with downstream dimethylbutane removal
摘要 <p>In the present invention, dimethylbutanes are removed from the raffinate component of the feed to a dehydrocyclization process. Thus, according to a preferred embodiment, a process is provided for producing aromatics by the following steps: (a) contacting fresh paraffins rich feed hydrocarbons, containing 0.1 to 20.0 wt. % dimethylbutanes with a highly selective dehydrocyclization catalyst in a reaction zone, under dehydrocyclization reaction conditions, to convert paraffins to aromatics and obtain an aromatics rich effluent; (b) separating aromatics from the effluent to obtain an aromatics lean raffinate; (c) removing dimethylbutanes from the raffinate to obtain a raffinate of reduced dimethylbutane content; and (d) recycling the raffinate of reduced dimethylbutane content to the reaction zone. Preferably, the dehydrocyclization catalyst used is a nonacidic, monofunctional catalyst. Platinum on L zeolite is a particularly preferred highly selective dehydrocyclization catalyst for use in the process. &lt;IMAGE&gt;</p>
申请公布号 EP1010745(A1) 申请公布日期 2000.06.21
申请号 EP19980310451 申请日期 1998.12.18
申请人 CHEVRON CHEMICAL COMPANY LLC 发明人 WITTE, DAVID H.
分类号 C10G61/02;C07C5/41;(IPC1-7):C10G61/02 主分类号 C10G61/02
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