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Method to control a CO2 chemical absorption system and CO2 chemical absorption system

机译:控制二氧化碳化学吸收系统的方法和二氧化碳化学吸收系统

摘要

A method for controlling a CO2 chemical absorption system, comprising a CO2 chemical absorption equipment and an absorbent generation equipment, the method comprising: (a) removing sulfur oxides in an exhaust gas discharged from an exhaust gas equipment. combustion (1) of fossil fuel by a flue gas desulfurization device (5) to obtain a desulfurized exhaust gas containing carbon dioxide (CO2), (b) contacting an amine absorbent with the desulfurized exhaust containing CO2 in a CO2 absorbing column (20) to absorb the CO2 in the amine absorber and obtain an amine absorber that has absorbed CO2, (c) heating the amine absorber that has absorbed CO2 in a column CO2 desorption (40) to release CO2 from the CO2 absorbed amine absorber and obtain a CO2 released amine absorber, (d) cool the CO2 released from CO2 absorbed amine absorber to separate a condensed water, (e) circulating the condensed water to the CO2 desorption column, (f) heating the CO2 released amine absorbent through a heat exchanger (60) for circulation to the CO2 desorption column, (g) heat exchange of the amine absorber released from CO2 extracted from the CO2 desorption column, with the amine absorber that has absorbed CO2 to be supplied to the CO2 desorption column, for circulation to the CO2 desorption column, (h ) extraction of the amine absorbent released from CO2 from the CO2 desorption column to the regenerator (94) of the absorbent regeneration equipment, (i) redirecting part of the condensed water to a buffer tank (83) of the regeneration equipment absorbent, (j) prepare an inorganic alkaline salt solution using the condensed water from the buffer tank, (k) add the inorganic alkaline salt solution to the CO2 released amine absorbent extracted from the CO2 desorption column, (l)removing heat stable salts accumulated in the CO2 released amine absorbent by a distillation process in the regenerator, (m) supplying CO2 released amine absorbent vapor resulting from the distillation process from the regenerator to the desorption column of CO2.
机译:一种用于控制CO 2化学吸收系统的方法,包括CO 2化学吸收设备和吸收剂产生设备,该方法包括:(a)去除从排气设备排出的排气中的硫氧化物。通过烟气脱硫装置(5)燃烧(1)化石燃料以获得含二氧化碳(CO2)的脱硫废气,(b)使胺吸收剂与含CO2的脱硫废气在CO2吸收塔(20)中接触在胺吸收器中吸收CO2并获得吸收了CO2的胺吸收器,(c)在柱CO2解吸中加热已吸收CO2的胺吸收器(40),从吸收了CO2的胺吸收器中释放CO2并获得CO2释放的胺吸收剂,(d)冷却吸收了CO2的胺吸收剂释放的CO2以分离冷凝水,(e)将冷凝水循环到CO2脱附塔,(f)通过热交换器加热释放出CO2的胺吸收剂(60 )循环到CO2解吸塔,(g)从CO2解吸塔提取的CO2释放出的胺吸收剂与吸收了CO2的胺吸收剂进行热交换,以供循环进入CO2解吸塔,(h)将从CO2解吸塔从CO2释放的胺吸收剂提取到吸收剂再生设备的再生器(94),(i)将部分冷凝水重定向到缓冲罐(83) )的再生设备吸收剂,(j)使用来自缓冲罐的冷凝水制备无机碱性盐溶液,(k)将无机碱性盐溶液添加到从CO2解吸塔提取的CO2释放的胺吸收剂中,(l)通过在再生器中的蒸馏过程除去累积在释放CO 2的胺吸收剂中的热稳定盐,(m)将由蒸馏过程产生的释放CO 2的胺吸收剂蒸气从再生器供应到CO 2的解吸塔。

著录项

  • 公开/公告号ES2671579T3

    专利类型

  • 公开/公告日2018-06-07

    原文格式PDF

  • 申请/专利权人 MITSUBISHI HITACHI POWER SYSTEMS LTD;

    申请/专利号ES20120747482T

  • 发明设计人 SHIMAMURA JUN;

    申请日2012-02-14

  • 分类号B01D53/62;B01D53;B01D53/14;B01D53/34;B01D53/50;B01D53/77;

  • 国家 ES

  • 入库时间 2022-08-21 12:48:30

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