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Numerical modeling of in-furnace sulfur removal by sorbent injection during pulverized lignite combustion

机译:褐煤粉燃烧过程中吸附剂注入炉内脱硫的数值模拟

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Results of the study on SO2 reduction in a utility boiler furnace by means of furnace sorbent injection are presented in this paper with analysis of major influential parameters. The Ca-based sorbent injection process in pulverized lignite fired boiler furnace with tangentially arranged burners is simulated. In simulations sorbent particles are distributed among the burner tiers, where they are injected together with coal, and also through sorbent injection ports located above the burners. The sorbent reactions model was adapted to be efficiently implemented in the code for CFD simulations of complex processes considering both the calculation time and the results accuracy. The sorbent particles reaction model was simplified with several assumptions to allow for faster calculations and significantly reduce simulation time without loss in calculation precision during the particle tracking in boiler furnace. Two phase gas-particle flow is modeled, with coal and sorbent particles reactions and interactions with gaseous phase. Test-cases based on fuels with different composition and combustion organization were simulated in details, and results showed that significant increase in reduction of SO2 at furnace exit could be achieved by proper sorbent injection. The sorbent injection locations were analyzed with special care to enable maximum SO2 capture in the case-study furnace under investigated conditions. Most of the test-cases with low SO2 capture had one or more of the following problems: intensive particle sintering, low local temperatures (leading to low calcination rates), or bad particles distribution. Significant SO2 retention was possible when the process was organized in such a way that particles were exposed to optimal temperature range, and injected in the furnace zones with high SO2 concentration simultaneously. It was shown that better results can be achieved by injection of sorbent through multiple burner tiers, with SO2 emission reduction efficiency around 60% at the furnace exit in several well optimized test-cases. (C) 2018 Elsevier Ltd. All rights reserved.
机译:通过对主要影响参数的分析,介绍了利用锅炉吸附剂注入法对电站锅炉炉内二氧化硫进行还原的研究结果。模拟了切向布置燃烧器的粉煤燃烧锅炉炉内钙基吸附剂的注入过程。在模拟中,吸附剂颗粒分布在各个燃烧器层之间,在此处与煤一起喷射,也通过位于燃烧器上方的吸附剂注入口喷射。考虑到计算时间和结果准确性,适用于在复杂过程的CFD模拟中有效地实施吸附剂反应模型。吸附剂颗粒反应模型通过几个假设进行了简化,以实现更快的计算并显着减少模拟时间,而不会在锅炉窑炉中跟踪颗粒时降低计算精度。用煤和吸附剂颗粒的反应以及与气相的相互作用对两相气体-颗粒流进行建模。详细地模拟了基于具有不同组成和燃烧组织的燃料的测试案例,结果表明,通过适当的吸附剂注入可以显着增加炉膛出口处的SO2还原量。要特别仔细地分析吸附剂的注入位置,以在案例研究炉中在调查条件下最大程度地捕获SO2。大多数具有低SO2捕获的测试用例都具有以下一个或多个问题:密集的颗粒烧结,较低的局部温度(导致较低的煅烧速率)或不好的颗粒分布。当该过程的组织方式使得颗粒暴露于最佳温度范围并同时以高SO2浓度注入炉膛时,可能会显着保留SO2。结果表明,通过在多个燃烧器层中注入吸附剂可以获得更好的结果,在几个经过优化的测试案例中,炉膛出口处的SO2减排效率约为60%。 (C)2018 Elsevier Ltd.保留所有权利。

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