首页> 外国专利> ISOMERIZATION OF C5 AND C6 PARAFFIN UTILIZING DISTILLATION ZONE WHERE RAW MATERIAL AND PRODUCT ARE UNITED

ISOMERIZATION OF C5 AND C6 PARAFFIN UTILIZING DISTILLATION ZONE WHERE RAW MATERIAL AND PRODUCT ARE UNITED

机译:结合原材料和产品的C5和C6石蜡利用蒸馏区的异构化

摘要

PURPOSE: To efficiently improve an octane number and to obtain a product which is useful as lead-free automobile fuel in good yielding at low cost by separating and distilling a low- boiling-point and a high-boiling-point component obtained by separating a lower hydrocarbon containing feed raw material in a distilling zone after processing them in an isomerizing zone and a reforming zone respectively. ;CONSTITUTION: The feed raw material 2 containing 5-7C hydrocarbons are sent in a splitter column as the 1st column of the distilling zone 1 consisting of the 1st column 21 and a 2nd column 22 and distilled, the low-boiling-point component 6 as a side-cut distillation is led to the isomerizing zone 5 and brought into contact with an isomerizing catalyst under isomerizing conditions so selected as to increase the octane numbers of the 5-6C components, and the reaction product is sent to a separating drum 13; and a rich-hydrogen off gas stream 14 is circulated to the isomerizing zone 5, a condensed liquid 16 is sent to a stabilizer 17 to extract a light component from the column top, and a column bottom stream 18 containing a high-octane-value product is returned to the distilling zone 1. A heavy hydrocarbon stream 4 as the high-boiling-point stream, on the other hand, is sent from the bottom of the column 21 to the reforming zone 3, the condensate 10 obtained by separating the reaction product by the separating drum 7 is led to the stabilizer to extract a light component from the column top, and a product 20 having a high octane number is obtained from the column bottom.;COPYRIGHT: (C)1989,JPO
机译:目的:通过分离和蒸馏分离出的低沸点和高沸点成分,有效地提高辛烷值,并以低成本高收率获得可用作无铅汽车燃料的产品。分别在异构化区和重整区进行处理后,在蒸馏区将低级含烃原料进料。 ;组成:将含有5-7C碳氢化合物的原料原料2送入作为第一区21和第二区22组成的蒸馏区1的第一级的分离塔,并进行蒸馏,将其低沸点成分6当将侧馏分馏出物引入异构化区5并在异构化条件下与异构化催化剂接触时,将其选择为增加5-6C组分的辛烷值,并将反应产物送入分离鼓13 ;富氢废气流14循环至异构化区5,冷凝液16被送入稳定器17以从塔顶提取轻组分,并且塔底流18包含高辛烷值产物返回到蒸馏区1。另一方面,作为高沸点物流的重质烃物流4从塔21的底部送至重整区3,通过分离重油获得冷凝液10。分离鼓7将反应产物通入稳定剂以从塔顶提取轻组分,并从塔底获得具有高辛烷值的产物20。COPYRIGHT:(C)1989,JPO

著录项

  • 公开/公告号JPH0553195B2

    专利类型

  • 公开/公告日1993-08-09

    原文格式PDF

  • 申请/专利权人 UOP INC;

    申请/专利号JP19880100027

  • 发明设计人 FUREDERITSUKU EMU HITSUBUZU;

    申请日1988-04-22

  • 分类号C10G61/02;C10G45/58;

  • 国家 JP

  • 入库时间 2022-08-22 05:21:04

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号