首页> 外国专利> System for recovery of acetic acid during the production of terephthalic acid, comprises dehydration column using azeotropic distillation to recover acetic acid in conjunction with condenser system to recover energy

System for recovery of acetic acid during the production of terephthalic acid, comprises dehydration column using azeotropic distillation to recover acetic acid in conjunction with condenser system to recover energy

机译:用于在对苯二甲酸生产过程中回收乙酸的系统,包括使用共沸蒸馏以回收乙酸的脱水塔以及与冷凝器系统结合以回收能量的脱水塔

摘要

The system comprises dehydration column using azeotropic distillation to recover the acetic acid in conjunction with a condenser system to recover energy. The column operates a dehydration pressure of 1.2 or higher in kilogram per square centimeter head of the column. The condenser system is a steam generator that condenses the vapor concentrated acetic acid to generate low-pressure steam from 0.6 to 250 kilogram per square centimeter. An independent claim is also included for a distillation method for recovery of acetic acid during the production of terephthalic acid.
机译:该系统包括使用共沸蒸馏以回收乙酸的脱水塔以及与冷凝器系统结合以回收能量的脱水塔。该塔的脱水压力以每平方厘米塔顶的千克计为1.2或更高。冷凝器系统是一种蒸汽发生器,它冷凝蒸汽浓缩的乙酸,以产生每平方厘米0.6至250千克的低压蒸汽。还包括用于在对苯二甲酸生产期间回收乙酸的蒸馏方法的独立权利要求。

著录项

  • 公开/公告号ES2302470A1

    专利类型

  • 公开/公告日2008-07-01

    原文格式PDF

  • 申请/专利权人 AMT INTERNATIONAL INC.;

    申请/专利号ES20060050012

  • 发明设计人 JANG JI-YOUNG;KIM HYUNG-JIN;WU KUANG;

    申请日2003-08-12

  • 分类号C07C51/46;B01D3/36;

  • 国家 ES

  • 入库时间 2022-08-21 20:04:13

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