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    循环流化床半干法脱硫装置烟道流场模拟优化

    Flue flow field simulation and optimization in CFB semi-dry desulfurization plant

    • 摘要: 循环流化床锅炉炉内脱硫无法满足排放要求时,需要对排烟进行进一步净化。烟气净化工艺主要有石灰石-石膏湿法烟气脱硫和循环流化床半干法烟气脱硫。为了比较2种工艺的经济性,建立了技术经济分析模型,对比分析了满负荷时炉内脱硫效率70%条件下的经济技术指标。分析结果表明,循环流化床半干法烟气脱硫的运行成本和总成本相对较低时,要求硫含量分别低于1.1%和2.1%;循环流化床半干法烟气脱硫的脱硫剂成本占比较大,而石灰石-石膏湿法烟气脱硫的电费占比相对略大;石灰石价格、上网电价和年运行时间是影响脱硫成本的主要因素,石灰石对脱硫成本的敏感度大于上网电价;石灰石价格低于112元/t时,石灰石-石膏湿法烟气脱硫的运行成本更高;上网电价低于0.43元/kWh时,石灰石-石膏湿法烟气脱硫的运行成本相较更低;循环流化床半干法烟气脱硫总成本在石灰石价格、电价、年运行时间的研究波动范围内相对较小;相较于常规炉内脱硫技术,超细石灰石炉内脱硫技术的炉内脱硫成本较低,与循环流化床半干法烟气脱硫工艺相结合的综合优势更显著。

       

      Abstract: Flow field characters have influential impacts on the improvement of desulfurization efficiency and system stability in the circulating fluidized bed semi dry desulfurization system,among whichthe uniformity and stability of the flow field are two key points of the whole system. Only when the design of fluidized bed and conveying equipment are reasonable,the stable and efficient operation of the desulfurization system can be guaranteed. Using CFD method and taking a semi-dry desulfurization plant of 300 MW coal-fired unit as the research objectives,and based on the calculation of the flue gas field in the desulfurization tower area and flue behind the dust collector,the non-uniformity of the flue gas flow field in the semi dry desulfurization system and improvement methods were investigated. Two models were established in the experiment. Model A is from the header of the 4 trumpet outlets of the pre-dust collector to the entrance of the bag dust collector,which is the main desulfurization reaction area. Model B is from the outlet of the bag filter to the inlet header of the induced draft fan and the main purpose of this area optimization is to reduce system resistance. Computational fluid dynamics simulation has been taken for analyzing placement and the number of guide vane as factors affecting flue flow field,velocity vector and pressure field. The result of optimization showed that the uniformity of the flow field can be improved by the application of the expansion header at the outlet of the pre-dust collector in model A. However,it is necessary to consider the ash accumulation caused by the reduction of the expansion flow rate,adjust the design of the ash accumulation load of the flue and steel structure and improve safety margin. A deflector blade is installed at the bottom of the desulfurization tower,which can effectively solve the bias problem and ensure the uniformity of the flue gas velocity entering the venturi,and the system resistance is also well controlled. The total resistance is around 2 200 Pa. The main optimization element of the bag flue outlet flue( model B) is to reduce the system resistance. The guide vane at the elbow 1 can effectively improve the speed distribution and reduce the resistance of the flue. When the number of guide vanes is 1-2,the effect is poor. When the number of guide vanes exceeds 3,the resistance basically reaches the optimal value and the air flow distribution is apparently improved. The guide vanes at the elbow 2 have little effect on reducing the resistance and improving the uniformity of flue gas flow field.

       

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