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    电站锅炉SCR烟气脱硝系统优化数值模拟

    Numerical Simulation on Optimization of SCR Denitrification System for Coal-fired Boilers

    • 摘要: 针对某电厂300 MW锅炉的选择性催化还原(SCR)反应系统,采用计算流体力学软件对不同结构下SCR反应器的脱硝特性进行了数值模拟,分析了导流板布置对SCR反应器内流场分布均匀性的影响,研究了不同布置方案下SCR反应器内氨氮物质的量比(简称氨氮比)分布的规律.结果表明:烟道内无导流板时,SCR反应器内的流场和NH3体积分数分布严重不均,SCR反应器的脱硝效率较低,氨逃逸率较高;采用初始方案,SCR反应器内的流场改善较大,但是第一层催化剂入口处氨氮比分布偏差大于5%;采用最终方案,第一层催化剂入口处的速度偏差为3.84%,氨氮比分布偏差为3.79%,SCR反应器的脱硝效率达到83%,NH3逃逸率低于5×10-6.

       

      Abstract: Taking the selective catalytic reduction (SCR) reaction system of a 300 MW coal-fired boiler as an example, numerical simulation was made to the denitration characteristics of the SCR reactor with different structures by fluid mechanics calculation software, so as to analyze the effects of guide plate layout on distribution of both the flow field and the ammonia-nitrogen ratio in the SCR reactor. Results show that both the flow field and NH3 volume fraction within the SCR reactor are severely uneven, the denitration efficiency of SCR reactor is relatively low and the ammonia escape rate is relatively high, when there is no guide plate installed in the flue; by adopting the initial solution, the flow filed in the SCR reactor is improved greatly, but the deviation of ammonia-nitrogen ratio distribution at inlet of the first catalyst layer is more than 5%; whereas, in the final solution, the deviation of velocity distribution at inlet of the first catalyst layer is 3.84%, where the deviation of ammonia-nitrogen ratio distribution is 3.79%, the denitration efficiency of SCR reactor reaches 83%, and the NH3 escape rate is lower than 5×10-6

       

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