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Simulation of power and cooling generation via heat recovery from a ventilation air methane abatement unit

机译:通过通风甲烷减排单元的热回收模拟发电和制冷

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摘要

Heat recovery from a fluidised-bed ventilation air methane abatement reactor and conversion into power using a Rankine cycle based steam turbine and cooling via an absorption chiller was simulated using the process simulation package Aspen Plus. The primary aim of the simulation was to determine the minimum methane concentration for self-sustaining operation, both in terms of maintaining the oxidation process at high temperature and to generate sufficient power to operate the plant. For a ventilation air flow rate of 20 m(3)/s (equivalent to a single abatement module), the minimum methane concentration was found to be 0.46 vol% at a reactor temperature of 650 degrees C and ambient pressure. The Rankine cycle operated with a steam pressure of 7.0 bar and steam flow rate of 0.4 kg/s. At the minimum methane concentration the process was self-sustained with zero net power being produced. The cooling produced at 0.46 vol% was 680 kW(R) using an indirect-fired absorption chiller while 780 kW(R) was produced via a direct-fired absorption chiller. Assuming a total ventilation air flow rate of 300 m(3)/s, fifteen 20 m(3)/s modules would be required, producing a total of up to 11,700 kW(R) of cooling.The net power produced was zero between reactor temperatures of 500 and 700 degrees C at the investigated steam pressures (2.0-7.0 bar). Excess net power was produced at reactor temperatures greater than 700 degrees C due to the restriction of the inlet VAM temperature to 600 degrees C (to prevent auto-ignition of the methane upstream of the reactor). At low reactor temperatures the steam flow rate decreased with both reactor temperature and steam pressure but remained constant at reactor temperatures of 750 and 800 degrees C.The methane abatement plant would be able to operate without an external power supply through the utilisation of the process heat. The plant would produce adequate cooling for a typical gassy underground coal mine in Australia. Such mines are located in the Bowen Basin of Queensland; a region characterised by high virgin rock temperatures with cooling requirements of up to 7000 kW(R).
机译:从流化床通风空气甲烷减排反应器中回收热量,并使用基于兰金循环的蒸汽轮机将其转化为电能,并使用过程模拟软件包Aspen Plus对通过吸收式冷却器进行的冷却进行了模拟。模拟的主要目的是确定自我维持操作的最低甲烷浓度,既要保持高温下的氧化过程,又要产生足够的能量来运行工厂。对于20 m(3)/ s的通风空气流量(相当于单个减排模块),发现在650摄氏度的反应堆温度和环境压力下,最低甲烷浓度为0.46体积%。朗肯循环以7.0巴的蒸汽压力和0.4kg / s的蒸汽流量运行。在最低甲烷浓度下,该过程可自我维持,产生的净功率为零。使用间接燃烧吸收式冷却器以0.46vol%产生的冷却为680 kW(R),而通过直接燃烧吸收式冷却器产生780 kW(R)。假设总通风空气流量为300 m(3)/ s,则需要15个20 m(3)/ s模块,产生的制冷量总计高达11,700 kW(R)。在研究的蒸汽压力(2.0-7.0 bar)下,反应器温度为500和700摄氏度。由于入口VAM温度限制在600摄氏度(以防止反应器上游的甲烷自燃),在高于700摄氏度的反应堆温度下产生了过量的净功率。在低反应堆温度下,蒸汽流速随反应堆温度和蒸汽压力的增加而降低,但在750和800摄氏度的反应堆温度下保持恒定。通过利用过程热,甲烷减排工厂无需外部电源即可运行。该工厂将为澳大利亚典型的瓦斯地下煤矿提供足够的冷却。这些地雷位于昆士兰州的博恩盆地。该地区的原始岩石温度高,冷却要求高达7000 kW(R)。

著录项

  • 来源
    《Fuel》 |2019年第1期|27-35|共9页
  • 作者单位

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

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

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

    Univ Newcastle, Chem Engn, 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);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Ventilation air methane; Heat recovery; Steam turbine; Absorption refrigeration; Aspen Plus;

    机译:甲烷通风;热回收;汽轮机;吸收式制冷;Aspen Plus;

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