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Combustion System Modelling of a Cracking Furnace to Reduce NOx Emissions

机译:裂解炉降低NOx排放的燃烧系统建模

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Linde was contracted to design and erect a new furnace section by BP in Gelsenkirchen.One of the key drivers for the project was compliance with the German clean air regulation "TALuft" respective to NOx emission (100 mg/Nm3 equiv. 0.058 #/MM BTU). The burners hadshown good emission performance in the test facilities of the burner supplier. However, atstart-up the emissions were significantly above the permitted levels. Shut down of thefurnaces to remedy was not an option due to high cost of lost production.A CFD model was set up and tuned to understand the differences between the testfacilities and the furnace installation at site. It could be shown that the high NOx level was dueto a "flame roll-over" which, in turn, was caused by excessive internal flue gas recirculation.Simulations showed that changes in burner tip drillings would provide improvement. As soonas the NOx predictions could qualitatively be re-produced at the furnace, additionaladaptations at the burner tile were investigated. A promising forecast was simulated for acontraction of the recirculation channels within the burner tiles; BP and Linde decided to applythis approach to one of the furnaces during a scheduled furnace shut-down.The combination of both, adapting the burner tips and contracting the recirculation flowpath solved the NOx problem and has been applied to all five furnaces in 2008. The NOxfigures recorded at the furnaces are now in the range of 75 – 90 mg/Nm3 (equiv. 0.04 – 0.052#/MM BTU).
机译:BP委托林德(Linde)在盖尔森基兴(Gelsenkirchen)设计和安装新的熔炉段。 该项目的主要推动力之一是遵守德国清洁空气法规“ TA 分别对应于NOx排放(100 mg / Nm3等效于0.058#/ MM BTU)。 在燃烧器供应商的测试设施中显示出良好的排放性能。但是,在 启动时的排放量大大高于许可水平。关机了 由于损失的生产成本高昂,因此无法选择炉子进行补救。 建立并调整了CFD模型以了解测试之间的差异 设施和现场熔炉安装。可以证明高NOx水平是由于 导致“火焰翻滚”,这又是由于内部烟道气再循环过多引起的。 模拟表明,燃烧器尖端钻孔的变化将提供改进。尽快 因为可以在炉子上定性地重现NOx的预测,因此 研究了燃烧器砖的适应性。对一个有希望的预测进行了模拟 燃烧器砖内的再循环通道收缩; BP和林德决定申请 在计划的炉子关闭期间,对其中一个炉子采用这种方法。 两者结合使用,可适应燃烧器喷嘴并减少再循环流量 路径解决了氮氧化物的问题,并已在2008年应用于所有五个熔炉。氮氧化物 现在,在熔炉上记录的数字范围是75 – 90 mg / Nm3(相当于0.04 – 0.052) #/ MM BTU)。

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