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Integration of a Coal-Fired Power Plant with an Ammonia-Based CO_2 Capture Process in Three Operation Modes

机译:三种运行模式下燃煤电厂与基于氨的CO_2捕集工艺的集成

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摘要

The techno-economic performance of a coal fired power plant integrated with postcombustion capture is affected by not only the capture system but also the way the power plant is operated. The existing integration studies typically use amines as the CO2 capture absorbent. However, amines will degrade in the capture process and produce harmful substances. Ammonia is a robust, low-cost alternative solvent for reducing CO2 emissions from coal-fired power plants. On the basis of a 660 MW coal-fired power plant, this study analyzes the performance of the integration of coal-fired power plant with an ammonia based CO2 capture process in three operation modes which include (1) reduction of power plant output compared to the original power station without CO2 capture and 85% CO2 capture efficiency, (2) the same power output as the original power station without CO2 capture and the same CO2 capture rate as in (1), and (3) the same power output as the original power station without CO2 capture and 85% CO2 capture efficiency. In each of three operation modes, we also analyzed the effect of stream extraction with and without auxiliary equipment energy consumptions in the CO2 capture process on the energy performance of the power plant. Results show that operation mode 2 exerts the least energy penalty on the power plant, but captures less CO2. On the premise of capturing as much CO2 as possible, operation mode 3 is the optimal operating mode, but the boiler and high-pressure cylinder require modification. Operation mode 3 is used as an example to analyze the effect of the solvent regeneration heat duty and temperature on the performance of the power plant. A decrease in heat duty is found to increase the system thermal efficiency and reduce the coal consumption rate and energy penalty. Lowering regeneration temperature while keeping the heat duty unchanged will improve the thermal efficiency of the system and reduce the coal consumption rate and energy penalty.
机译:与燃烧后捕集相结合的燃煤电厂的技术经济性能不仅受捕集系统的影响,还受电厂运行方式的影响。现有的集成研究通常使用胺作为CO2捕获吸收剂。但是,胺会在捕获过程中降解并产生有害物质。氨是一种强大的低成本替代溶剂,可减少燃煤电厂的二氧化碳排放。以660兆瓦的燃煤电厂为基础,本研究分析了三种运行模式下燃煤电厂与氨基CO2捕集工艺的集成性能,其中包括(1)与没有CO2捕集且CO2捕集效率达到85%的原始电站,(2)与没有CO2捕集的原电站相同的功率输出,且与(1)中相同的CO2捕集率,以及(3)与原始电站没有二氧化碳捕集,二氧化碳捕集效率达到85%。在这三种操作模式的每一种中,我们还分析了在有或没有辅助设备能耗的情况下,在二氧化碳捕集过程中进行流萃取对电厂能源性能的影响。结果表明,运行模式2对发电厂的能耗损失最小,但捕获的二氧化碳更少。在尽可能多地捕获CO2的前提下,最佳运行模式是运行模式3,但是锅炉和高压缸需要修改。以运行模式3为例,分析了溶剂再生热负荷和温度对电厂性能的影响。发现降低热负荷可提高系统热效率,并减少煤炭消耗率和能耗。在保持热负荷不变的情况下降低再生温度将提高系统的热效率,并减少煤炭消耗率和能耗。

著录项

  • 来源
    《Energy & fuels》 |2018年第10期|10760-10772|共13页
  • 作者单位

    North China Elect Power Univ, Sch Energy Power & Mech Engn, Beijing 102206, Peoples R China;

    CSIRO Energy, 10 Murray Dwyer Circuit, Mayfield West, NSW 2304, Australia;

    North China Elect Power Univ, Sch Energy Power & Mech Engn, Beijing 102206, Peoples R China;

    North China Elect Power Univ, Sch Energy Power & Mech Engn, Beijing 102206, Peoples R China;

    CSIRO Energy, 10 Murray Dwyer Circuit, Mayfield West, NSW 2304, Australia;

    North China Elect Power Univ, Sch Energy Power & Mech Engn, Beijing 102206, Peoples R China;

  • 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
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