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首页> 外文期刊>Energy & fuels >Thermodynamic Assessment of Heat Recovery from a Fluidized-Bed Ventilation Air Methane Abatement Unit
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Thermodynamic Assessment of Heat Recovery from a Fluidized-Bed Ventilation Air Methane Abatement Unit

机译:从流化床通风甲烷减排装置回收热量的热力学评估

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摘要

Methane, a greenhouse gas, is the second largest contributor to global warming after carbon dioxide and is 25 times more effective at trapping heat in the atmosphere than carbon dioxide. In 2015, fugitive emissions of methane from Australian underground coal mines were reported at 25 million tonnes of carbon dioxide equivalent. Ventilation air methane (VAM) is present in low concentrations (below 1.0 vol %), and its abatement and use as an energy source are a challenge for the coal mining industry. This paper examines the recovery of heat from a fluidized-bed VAM abatement unit and utilization in power generation via the Brayton cycle. The objective of the study was to determine the minimum methane concentration required to maintain autothermal operations and produce sufficient power to operate a fluidized-bed plant without supplementary power or fuel. Four configurations were studied and simulated using Aspen Plus software. For direct heat recovery, the minimum methane concentration increased with an increase in both the reactor outlet temperature and compressor outlet pressure. The minimum methane concentration for the indirect heat recovery configurations decreased when both the reactor outlet temperature and compressor outlet pressure increased. For all configurations, the minimum methane concentration was limited by the maximum reactor inlet temperature of 600 degrees C (to prevent autoignition of methane upstream of the reactor).
机译:甲烷是一种温室气体,是仅次于二氧化碳的全球第二大温室气体排放者,其在空气中的散热效率是二氧化碳的25倍。据报道,2015年澳大利亚地下煤矿的甲烷逃逸排放量为2500万吨二氧化碳当量。通风空气甲烷(VAM)的浓度较低(低于1.0 vol%),其减排和用作能源对煤矿行业来说是一个挑战。本文研究了从流化床VAM减排装置回收的热量以及通过布雷顿循环在发电中的利用。这项研究的目的是确定维持自热运行并产生足够的能量来运行流化床设备而无需补充动力或燃料的最低甲烷浓度。使用Aspen Plus软件对四种配置进行了研究和仿真。对于直接热回收,最低甲烷浓度随反应器出口温度和压缩机出口压力的增加而增加。当反应器出口温度和压缩机出口压力均增加时,间接热回收配置的最低甲烷浓度降低。对于所有配置,最低甲烷浓度受到最大反应器入口温度600摄氏度的限制(以防止甲烷在反应器上游自燃)。

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  • 来源
    《Energy & fuels 》 |2018年第4期| 4579-4585| 共7页
  • 作者单位

    Univ Newcastle, Prior Res Ctr Frontier Energy Technol & Utilisat, Univ Dr, Callaghan, NSW 2308, Australia;

    Univ Newcastle, Prior Res Ctr Frontier Energy Technol & Utilisat, Univ Dr, Callaghan, NSW 2308, Australia;

    Univ Newcastle, Prior Res Ctr Frontier Energy Technol & Utilisat, Univ Dr, Callaghan, NSW 2308, Australia;

    Univ Newcastle, Prior Res Ctr Frontier Energy Technol & Utilisat, Univ Dr, Callaghan, NSW 2308, Australia;

  • 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
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