2.3MW加氢精制加热炉富氧燃烧特性的CFD模拟OA
CFD Simulation of Oxygen-Enriched Combustion Characteristics of 2.3 MW Hydrofining Heating Furnace
管式加热炉是炼油化工装置的关键供热单元和能耗大户.改善燃料的燃烧效果,提高加热炉的热效率,对炼油化工装置的节能减排具有一定的现实意义.以航空煤油加氢精制装置的管式加热炉为研究对象,采用计算流体动力学(CFD)模拟方法,基于标准k-ε湍流模型、组分输运燃烧模型以及P-1辐射模型,通过改变助燃空气中氧体积分数,分析了氧体积分数对现有加热炉的辐射室温度、炉管表面平均温度以及燃烧器炉嘴温度分布的影响.结果表明,当氧体积分数在18.55%~26.00%的范围内变化时,氧体积分数对炉内温度场和燃烧效率有显著影响,现有的加热炉辐射室、炉管和火嘴能完全满足富氧燃烧的需要.
The tubular heating furnace is a key heating unit and a major energy consumer in refinery and chemical plants.Improving fuel combustion efficiency and the thermal efficiency of the heating furnace is of practical significance for energy conservation and emission reduction in these facilities.In this paper,the tubular heating furnace of aviation kerosene hydrofining unit is studied.The computational fluid dynamics(CFD)simulation method is adopted,and the standard k-ε turbulence model,component transport combustion model and P-1 radiation model are used.The temperature of the furnace,the average temperature of the surface of the furnace tube and the temperature distribution of the burner were investigated by changing the oxygen content of the combustion air.The results indicate that when the oxygen volume fraction changes in the range of 18.55%-26.00%,the oxygen volume fraction change has a significant impact on the temperature field and combustion efficiency in the furnace,and the existing radiation chamber,furnace tube and burner fully meet the needs of oxygen-rich combustion..
赵德强;魏海龙;王甲麟;李刚;王良成
中国石油天然气股份有限公司 兰州石化分公司,甘肃 兰州 730060兰州交通大学 化学化工学院,甘肃 兰州 730070兰州交通大学 化学化工学院,甘肃 兰州 730070兰州交通大学 化学化工学院,甘肃 兰州 730070兰州交通大学 铁道车辆热工教育部重点实验室,甘肃 兰州 730070
能源科技
管式加热炉辐射室温度富氧燃烧CFD模拟氧体积分数
Tubular heating furnaceRadiant chamber temperatureOxygen-enriched combustionCFD simulationOxygen volume fraction
《辽宁石油化工大学学报》 2026 (3)
25-32,8
国家自然科学基金项目(52176074)兰州交通大学加热炉富氧燃烧技术开发项目(LZSH-2023-JS-210).
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