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two-stage aromatisation maximum simulated xylen - yield with split feed

机译:两阶段芳构化最大模拟二甲苯-分批进料的产率

摘要

A full boiling hydrocarbon feed is reformed to enhance para-xylene and benzene yields. First, the hydrocarbon feed is separated into a C5- cut, a C6-C7 cut, and a C8+ cut. The C6-C7 cut has less than 5 lv. % of C8+ hydrocarbon, and the C8+ cut has less than 10 lv. % of C7- hydrocarbon. The C6-C7 cut is subjected to catalytic aromatization at elevated temperatures in a first reformer in the presence of hydrogen and using a non-acidic catalyst comprising at least one Group VIII metal and a non-acidic zeolite support to produce a first reformate stream; and the C8+ cut is subjected to catalytic aromatization at elevated temperatures in a second reformer in the presence of hydrogen and using an acidic catalyst comprising at least one Group VIII metal and a metallic oxide support to produce a second reformate stream. Less than 20 wt.% of the total amount of C8 aromatics produced in the first and second reformer is ethylbenzene, and more than 20 wt.% of the total amount of xylenes produced in the first and second reformer are para-xylenes.
机译:重整全沸点烃进料以提高对二甲苯和苯的产率。首先,将烃进料分离为C5-馏分,C6-C7馏分和C8 +馏分。 C6-C7切工小于5 lv。 %的C8 +烃,并且C8 +馏分具有小于10lv。 C 7-烃的%。将C6-C7馏分在第一重整器中,在氢气存在下,在高温下,使用包含至少一种VIII族金属和非酸性沸石载体的非酸性催化剂,进行催化芳构化,以产生第一重整产物流;所述C 8+馏分在第二重整器中在氢气存在下在高温下进行催化芳构化,并使用包含至少一种VIII族金属和金属氧化物载体的酸性催化剂产生第二重整产物流。在第一和第二重整器中产生的C 8芳族化合物的总量的少于20重量%是乙苯,并且在第一和第二重整器中产生的二甲苯的总量的超过20重量%是对二甲苯。

著录项

  • 公开/公告号DE69715682D1

    专利类型

  • 公开/公告日2002-10-24

    原文格式PDF

  • 申请/专利权人 CHEVRON PHILLIPS CHEMICAL CO. LP HOUSTON;

    申请/专利号DE19976015682T

  • 发明设计人 NACAMULI J.;THOM J.;

    申请日1997-06-16

  • 分类号C10G59/06;

  • 国家 DE

  • 入库时间 2022-08-22 00:24:52

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