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ONE TOWER-MULTIBEDS CIRCULATING FLUIDIZATION LARGE-SCALE DRY DESULFURIZATING PROCESS FOR FLUE GAS

机译:一塔多床循环流化床大型干法烟气脱硫工艺

摘要

The present invention provides a large-scale dry desulfurizating process for flue gas, the process is based on an one tower-multibeds circulating fluidization technology. At the request of the large scale dry desulfurization for flue gas, the bottom fluidized region of the desulfurization reaction tower is divided into two or more independent small fluidized regions (fluidized subbeds),and above the fluidized subbeds at the bottom of the desulfurization tower, the independent small fluidized subbeds are organically combined into a desulfurization reaction tower with single tower structure. It solves the fluidizing problems of the desulphurizer particles when the single tower is scaled up, it solves the flow field organization problems of the multiphase chemical reaction process, and it solves the nuclear technology problems of the scaling-up the single tower for the circulation fluidized dry desulfurization for flue gas. At the same time, It can reduce the height of the large scale desulfurization tower, realizes the scaling-up of single tower in the dry desulfurization process for flue gas, and it reduce the cost of dry desulfurization for flue gas, it realizes the desulfurization technology needs of high desulfurization efficiencywide turndown ratio, low investment and low running cost, low water consumption.
机译:本发明提供了一种烟气的大规模干法脱硫工艺,该工艺基于单塔多床循环流化技术。根据烟气的大规模干法脱硫要求,将脱硫反应塔的底部流化区分为两个或更多个独立的小流化区(流化床),并在脱硫塔底部的流化床上方。独立的小型流化床层有机结合成具有单塔结构的脱硫反应塔。解决了单塔放大时脱硫剂颗粒的流化问题,解决了多相化学反应过程的流场组织问题,解决了单塔循环流化时放大的核技术问题。烟气的干法脱硫。同时,可以减小大型脱硫塔的高度,实现烟气干法脱硫工艺中单塔的放大,降低烟气干法脱硫的成本,​​实现脱硫技术要求脱硫效率高,调节比大,投资少,运行成本低,水耗低。

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