Numerical simulation of a circulating fluidized bed desulfurizing reactor with bypass
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摘要: 循环流化床半干法脱硫工艺中反应器的流场情况会影响脱硫效率。在保证文丘里管烟气速度不变的情况下,在反应器入口和扩散段之间设置跨过文丘里管段的旁路装置,来适应不同烟气量负荷变化的方式,不仅能优化反应器内流场,还有利于脱硫效率的提高。数值模拟结果表明:反应器烟气量负荷变化时,旁路阀门的开度需>50%且旁路管道的数量不少于2个,才能保证反应器内流场的均匀分布。带旁路循环流化床反应器在烟气量负荷为100%时空塔压力损失为911 Pa,随着负荷降低,空塔压力损失减少至500 Pa左右。综上,通过旁路结构的引入与优化调控,带旁路循环流化床脱硫反应器能在50%~100%的宽烟气负荷范围内实现均匀稳定的流场与较低的运行压损,为实际工程中提高脱硫效率与运行适应性提供有效解决方案。Abstract: In the semi-dry desulfurization process of the circulating fluidized bed, the flow field of the reactor usually affects its desulfurization efficiency. Under the condition of constant flue gas velocity in the Venturi tube, the measure for adapting to different flue gas load variation by setting bypass valves across the Venturi tube section between the reactor inlet and the diffusion section can not only optimize the flow field inside the reactor, but also improve the desulfurization efficiency. In this paper, through numerical simulation, it was concluded that, when the flue gas load of the reactor changes, the opening of the bypass valves should be no less than 50%, and the number of bypass pipelines should be no less than 2, to ensure the uniform flow field distribution in the reactor. When the flue gas load was 100%, the pressure loss of the reactor was 911 Pa. With the flue gas load decrease, the pressure loss of the empty reactor was about 500 Pa. In summary, the circulating fluidized bed reactor with a bypass through the introduction and optimized regulation of the bypass structure, can achieve uniform and stable flow fields as well as low operating pressure losses within a wide flue gas load range of 50% to 100%. This provides an effective solution for enhancing desulfurization efficiency and operational adaptability in practical engineering applications.
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Key words:
- circulating fluidized bed /
- desulfurizing /
- bypass device /
- reactor /
- numerical simulation /
- iron and steel plant
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