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Process for CO_2 Capture Using Ionic Liquid That Exhibits Phase Change

机译:使用表现出相变的离子液体捕获CO_2的方法

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摘要

A novel process for capturing carbon dioxide from the flue gas of a coal-fired power plant has been shown to reduce parasitic power consumption substantially. The process employs an ionic liquid created at the University of Notre Dame that has a high capacity for absorbing CO_2 by chemical reaction. A distinguishing property of this ionic liquid is that it changes phase from solid to liquid upon reaction with CO_2. The process uses heat generated by this phase transition to lower parasitic power consumption. The driving force for CO_2 separation is a combination of temperature and pressure differences; the process could even work without the addition of heat A realistic process was created to capture CO_2 efficiently. Computer simulation of the process enabled calculation of viable process conditions and power usage. The main concepts of the process were shown to work using a lab-scale apparatus. Parasitic power consumes 23% of net power generation, 55% lower than that of the monoethanolamine (MEA) process. However, capital cost is higher. The cost of electricity (COE) is 28% lower than that of the MEA process.
机译:从燃煤发电厂的烟气中捕获二氧化碳的新颖方法已显示出可大大减少寄生功率消耗。该方法采用由圣母大学创建的离子液体,该离子液体具有通过化学反应吸收CO_2的高容量。该离子液体的一个显着特性是,与CO_2反应后,离子液体从固态变为液态。该工艺使用了此相变产生的热量,以降低寄生功耗。分离CO_2的驱动力是温差和压差的结合。该过程甚至可以在不增加热量的情况下进行。创建了一个现实的过程来有效地捕获CO_2。对过程进行计算机仿真可以计算可行的过程条件和功耗。该过程的主要概念已显示为使用实验室规模的设备工作。寄生功率消耗净发电量的23%,比单乙醇胺(MEA)工艺的发电量低55%。但是,资金成本较高。与MEA工艺相比,电费(COE)降低了28%。

著录项

  • 来源
    《Energy & fuels》 |2014年第novaadeca期|7070-7078|共9页
  • 作者单位

    Mid-Atlantic Technology, Research & Innovation Center (MATRIC), Post Office Box 8396, South Charleston, West Virginia 25303, United States;

    Mid-Atlantic Technology, Research & Innovation Center (MATRIC), Post Office Box 8396, South Charleston, West Virginia 25303, United States;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

  • 入库时间 2022-08-18 00:40:31

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