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首页> 外文期刊>Energy Conversion & Management >An innovative process for simultaneous removal of CO_2 and SO_2 from flue gas of a power plant by energy integration
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An innovative process for simultaneous removal of CO_2 and SO_2 from flue gas of a power plant by energy integration

机译:通过能量整合同时从电厂烟气中去除CO_2和SO_2的创新工艺

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摘要

With the fast development of the society, the amount of carbon dioxide has been increased enormously in the atmosphere all over the world, which has already endangered the survival of human being. More and more people or organizations are studying new technologies to reduce the cost of capturing CO_2. The recovery and sequestration of CO_2 from flue gas of the power plant is regarded as a feasible way to mitigate the greenhouse gas emissions. Therefore, the process of recovering carbon dioxide by chemical absorption with monoethanolamine (MEA) in industry was emphatically described in this paper. Based on energy integration, a coupled process was proposed which included MEA absorption of CO_2 and SO_2, and the heat recovery from the flue gas's waste heat recovery unit and compressor inter-stage cooling unit. Compared the innovative process with an original process, 9% of thermal energy could be reduced in the new flowsheet. Meanwhile decarbonization and desulphurization could be carried on in the absorber simultaneously without the usual wet flue gas desulphurization (FGD) system. An exergy analysis model was established and validated by the literature data with a deviation less than 5.40%. The exergy results indicated that the exergy loss of the improved process was 15.48-20.75% less than that of the original one, which proved that the innovative process was reasonable and effective from the perspective of energy utilization.
机译:随着社会的快速发展,全世界大气中二氧化碳的数量大大增加,已经危及人类的生存。越来越多的人或组织正在研究新技术以降低捕获CO_2的成本。从电厂烟气中回收和封存CO_2被认为是减轻温室气体排放的可行方法。因此,本文着重介绍了工业上通过单乙醇胺(MEA)的化学吸收回收二氧化碳的过程。基于能量集成,提出了一种耦合过程,包括MEA吸收CO_2和SO_2,以及从烟气的废热回收单元和压缩机级间冷却单元回收热量。将创新工艺与原始工艺进行比较,可以在新流程中减少9%的热能。同时,在吸收塔中可以同时进行脱碳和脱硫,而无需通常的湿法烟气脱硫(FGD)系统。建立了火用分析模型,并通过文献数据验证了偏差小于5.40%。火用结果表明,改进工艺的火用损失比原始工艺减少了15.48-20.75%,从能源利用的角度证明了该工艺是合理有效的。

著录项

  • 来源
    《Energy Conversion & Management》 |2009年第12期|2885-2892|共8页
  • 作者单位

    State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, PR China;

    School of Energy and Power Engineering, Xi'an jiaotong University, Xi'an 710049, PR China;

    State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, PR China;

    State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, PR China;

    State Key Laboratory of Multiphase Flow in Power Engineering, Xi'an Jiaotong University, PR China School of Energy and Power Engineering, Xi'an jiaotong University, Xi'an 710049, PR China;

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

    carbon dioxide; sulfur dioxide; flue gas; compressor inter-stage cooling; energy integration; exergy analysis;

    机译:二氧化碳;二氧化硫;烟气压缩机级间冷却;能源整合;火用分析;

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