回收法氧化镁湿法烟气脱硫机理和工艺基础研究

Mechanism and Technology of Recovery Flue Gas Desulphurization with Magnesium Oxide

以氧化镁浆液作为吸收液，对空气与SO2混合气的鼓泡吸收做了全过程的实验观察．测试分析表明，在高效而稳定的脱硫过程中，吸收液的酸化是由HSO3^-所致；酸化趋势与SO2水解规律相一致，由初期高pH值下SO3^2-为主的缓变到低pH值下HSO3^-为主的剧变；吸收液温度对脱硫率的影响不敏感；MgSO3相对高的溶解度和易氧化性及MgSO4良好的水溶性保持了MgO脱硫的高效率（〉98％）和高利用率燃煤烟气脱硫工业试验确认了MgSO4经吸收液循环可提浓至实验温度（40～50℃）下的饱和浓度而不产生有害影响，脱硫率因脱硫活性物质的富集反而提高，从而显示出回收工艺的技术经济可行性。

Taking magnesium oxide slurry as absorption solution, the simulation of bubbling absorption process of mixed SO2 gases was observed in laboratory. Experiment results show that with a high efficiency and stable situation, acidification of absorbing .solution was caused by HSO3^- ; the acidification trend was in accordance with the pattern of hydrolyzing of SO2, pH changes slowly at high pH value with SO3^2- and rapidly at low value with HSO3^-. The experiments also show the insensitive effect of liquid temperature on the high desulphurization efficiency. With relatively high disolution rate and oxidizability of MgSO3 as well as the high solubility of MgSO4, the desulphurization efficiency utilization of MgO. Industrial experiment of FGD of coal fired boiler showed that by recycling absorbing liquid could be raised to the concentration of MgSO4 tO the saturation concentration at the operation temperature （40- 50℃ ）, without any adverse effects on FGD efficiency. Refinement and enrichment of active substance could promote the desulphurization process, thus showed the availability of technical and economy feasibility of recovery technology.