摘要
利用凹凸棒石(PG)负载V_2O_5制得V_2O_5/PG催化剂并将其用于脱除烟气中的Hg~0.在固定床反应器上研究了V_2O_5/PG催化剂脱除Hg~0的性能,考察了反应温度、汞浓度、空速、烟气成分等对V_2O_5/PG脱除Hg~0的影响,并利用傅里叶红外光谱、逐级化学提取和程序升温脱附实验分析了V_2O_5/PG上吸附Hg的形态.实验结果表明,V_2O_5/PG催化剂在120~210℃范围内、电厂烟气净化空速和所含汞浓度条件下具有良好的脱除Hg~0的能力.烟气成分对V_2O_5/PG脱除Hg~0的影响不同,O_2具有显著的促进作用,而SO_2和H_2O具有一定的抑制作用,NO和CO_2的作用不明显.O_2、SO_2和H_2O共同存在时,促进了Hg~0的脱除.傅里叶红外光谱、逐级化学提取和程序升温脱附实验的结果证实,V_2O_5/PG上吸附的汞存在不同形态,主要是Hg~(2+)的化合物,表明Hg~0在V_2O_5/PG上的脱除是吸附和催化氧化的共同作用,V_2O_5在V_2O_5/PG脱除Hg~0的过程中起到了关键作用.
A V_2O_5/PG catalyst, which was prepared by supporting V_2O_5 onto palygorskite(PG), was used to remove Hg~0 from flue gas in a fixed-bed reactor. The effects of temperature, Hg~0 concentration, space velocity and flue gas components on Hg~0 removal over V_2O_5/PG were studied. Furthermore, the speciation of Hg adsorbed over V_2O_5/PG catalyst was also characterized by FT-IR, sequential chemical extraction(SCE) and temperature programmed desorption(TPD) experiments. The results showed that V_2O_5/PG catalyst had a high Hg~0 removal capability in the temperature range of 120~210 ℃ within a space velocity and the Hg~0 concentration in flue gas of coal combustion power plant. O_2 showed a promotion effect on Hg~0 removal over V_2O_5/PG while SO_2 and H_2O showed an inhibition effect, NO and CO_2 showed no obvious effect. The co-effect of O_2, SO_2 and H_2O promoted Hg~0 removal by V_2O_5/PG. The results of FT-IR, SCE and TPD showed that there were different speciation of Hg over V_2O_5/PG and the main form was Hg~(2+) compounds. These confirmed that Hg~0 removal over V_2O_5/PG was the co-effect of adsorption and oxidation, in which the catalytic oxidation activity of V_2O_5 played a critical role, i.e. oxidizing Hg~0 to form Hg~(2+) compound.
引文
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