摘要
烟气中的汞分为单质汞(Hg^0)、氧化态汞(Hg^(2+))和颗粒态汞(Hg_p)三种形态,其中Hg_p可以被除尘装置捕集,Hg^(2+)易溶于水,易被湿法脱硫装置(WFGD)吸收,而Hg^0很难用常规方法有效脱除,是烟气中汞污染控制的难点。湿法脱硫系统捕集下来的Hg^(2+)会被浆液中的SO_3^(2-)还原生成Hg^0,导致WFGD脱汞效率下降。通过Aspen Plus模拟了WFGD的工艺流程,并建立了Hg-S-Cl体系的反应动力学模型,以此分析温度、SO2浓度、氯离子浓度和pH等参数对WFGD脱汞性能的影响。
Mercury in the flue gas occurs primarily in three forms: elemental (Hg0), oxi- dized mercury (Hg2+ ) and particle bound mercury (Hgp) , Hgp can be easily captured by par- ticulate matter control devices (PMCDs). Wet flue gas desulfurization (WFGD) can remove most of Hg2+ due to its water-soluble property. However, parts of Hg2+ would be reduced to Hg0by sulfite in desulfurization process, increasing the re-emission of mercury, which de- crease the removing mercury efficiency of WFGD. The simulation process of WFGD is estab- lished through the Aspen plus software, and a chemical kinetics model has been developed to describe the aqueous mercury sulfite-chloride-thiosulfate system and takes into account the simultaneous occurrence of a number of reaction steps. This work predicts the effects of tem- perature, reactant concentrations, pH, chloride, and thiosulfate on the rates of these reac- tions, and thus on the re-emission of Hg from WFGD systems.
出处
《锅炉技术》
北大核心
2016年第5期21-24,30,共5页
Boiler Technology