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Demonstration and its validation for ventilation air methane (VAM) thermal oxidation and energy recovery project

机译:通风甲烷热氧化和能量回收项目的演示及其验证

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In the present work, a preliminary technical and demonstration running assessment had been conducted in the Dafosi coal mine, China. First commercially available technologies for both mitigation and utilization of coal mine methane (VAM) combined with drained low concentration methane by premixing and co-oxidation was briefly described. Based on the methane emission characteristics, the running properties of thermal flow reversal reactor (TFRR) and gas mixing unit have been analyzed systemically. Under the experimental condition, TFRR should be preheated for about 27 h until the central temperature of monolith bed reaching to about 1000 degrees C. Another 9 h are needed to make the temperature evolutes to the similar profiles under the stable operation conditions with the help of electric heater and fed methane gas oxidation. For the TFRR, about 31.61%-46.82% energy can be recovered and used for electricity generation at the stable running conditions. Methane concentration corresponding to TFRR stable and self-maintained running should not be less than 0.25%. However, the effective and economical operation with heat recovery for electricity generation is possible only for the methane concentrations higher than 0.6%, and recommended at 1.0 vol.% methane concentration. (C) 2015 Elsevier Ltd. All rights reserved.
机译:在目前的工作中,已经在中国达佛斯煤矿进行了初步的技术和示范运行评估。简要介绍了通过预混和共氧化技术来缓解和利用煤矿瓦斯(VAM)与排放的低浓度瓦斯相结合的第一种商业可用技术。基于甲烷的排放特性,系统地分析了热逆流反应器(TFRR)和气体混合装置的运行特性。在实验条件下,应将TFRR预热约27 h,直到整料床的中心温度达到约1000摄氏度为止。在稳定运行条件下,还需要另外9 h使温度逐渐升高到相似的温度曲线。电加热器和进料甲烷的氧化。对于TFRR,可以在稳定的运行条件下回收约31.61%-46.82%的能量并用于发电。与TFRR稳定和自保持运行相对应的甲烷浓度应不小于0.25%。但是,只有在甲烷浓度高于0.6%且建议在甲烷浓度为1.0 vol%的情况下,才能进行有效而经济的热回收发电。 (C)2015 Elsevier Ltd.保留所有权利。

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