...
首页> 外文期刊>Fuel >Simulation of power and cooling generation via heat recovery from a ventilation air methane abatement unit
【24h】

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

机译:通过从通风空气甲烷减排单元进行热回收的电力和冷却产生模拟

获取原文
获取原文并翻译 | 示例

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:通过朗肯循环基汽轮机从流化床通风空气甲烷减排反应器中加热回收蒸汽涡轮和通过吸收冷却器的冷却,通过工艺模拟封装Aspen Plus进行模拟。模拟的主要目的是确定自我维持操作的最小甲烷浓度,无论是在高温下保持氧化过程,都可产生足够的动力以操作植物。对于通风空气流速为20μm(3)/ s(相当于单减排模块),发现最小甲烷浓度在650℃和环境压力的反应器温度下为0.46体积%。朗肯循环以7.0巴的蒸汽压力和0.4kg / s的蒸汽流量为操作。在最小甲烷浓度下,该方法具有零净功率的自体持续。使用间接烧制的吸收冷却器为0.46体积%的冷却为680kW(R),而通过直接烧制的吸收冷却器生产780kW(R)。假设总通气空气流量为300米(3)/ s,需要150米(3)/秒的模块,生产总共高达11,700千瓦(R)的冷却。所产生的净功率在零之间在调查的蒸汽压力下(2.0-7.0巴),电反应器温度为500和700℃。由于入口VAM温度为600℃的限制,在大于700℃的反应器温度下产生过多的净功率(以防止反应器上游的甲烷自动点火)。在低反应器温度下,蒸汽流速随着反应器温度和蒸汽压力而降低,但在750和800摄氏度的反应器温度下保持恒定。甲烷减排设备通过利用工艺热量而没有外部电源。 。该工厂将为澳大利亚典型的Gassy地下煤矿产生足够的冷却。这些地雷位于昆士兰州的鲍文盆地;具有高原始岩石温度的区域,具有高达7000千瓦(R)的冷却要求。

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:通风空气甲烷;热回收;蒸汽轮机;吸收制冷;aspen plus;

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号