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论文摘要

pH值缓冲剂及烟气氧含量对软锰矿浆烟气脱硫体系的影响

Influence of pH Buffer and Oxygen Concentration in Flue Gas on the System of Flue Gas Desulfurization with Pyrolusite Pulp

作者:孙峻(四川大学 环境科学与工程系 四川 成都 610065);苏仕军(四川大学 环境科学与工程系 四川 成都 610065);丁桑岚(四川大学 环境科学与工程系 四川 成都 610065)

Author:(Dept. of Environmental Sci. and Eng., Sichuan Univ., Chengdu 610065,China);(Dept. of Environmental Sci. and Eng., Sichuan Univ., Chengdu 610065,China);(Dept. of Environmental Sci. and Eng., Sichuan Univ., Chengdu 610065,China)

收稿日期:2006-10-20          年卷(期)页码:2007,39(4):73-78

期刊名称:工程科学与技术

Journal Name:Advanced Engineering Sciences

关键字:软锰矿;烟气脱硫;pH值缓冲剂; 烟气氧含量

Key words:pyrolusite pulp; flue gas desulfurization; pH value buffer; oxygen concentration of flue gas

基金项目:国家科技部资助项目(85-912-04-01-02);四川省重点科技攻关项目(05GG021-026-04);国家烟气脱硫工程技术研究中心资助项目(2001DC105003-1)

中文摘要

软锰矿浆烟气脱硫工艺能利用软锰矿中的MnO2与烟气中的SO2反应生成副产品硫酸锰,喷射鼓泡反应器(JBR)适宜于该工艺体系,但在单级JBR反应器中进行软锰矿浆烟气脱硫很难同时实现较高的脱硫率(η(SO2))和锰浸出率(X(Mn))。针对这一问题,通过实验在JBR反应器中考察了pH值缓冲剂添加比例和烟气氧含量对软锰矿浆烟气脱硫体系的影响,确定烟气氧含量为21%时pH值缓冲剂的最佳添加比例为30%,烟气氧含量为7%时pH缓冲剂的最佳添加比例为10%。结果表明,在模拟燃煤烟气的条件下,体系中pH值缓冲剂的添加比

英文摘要

The flue gas desulfurization with pyrolusite pulp can produce the byproduct of manganese sulfate from the corresponding chemical reaction between MnO2 in pyrolusite and SO2 in flue gas, and moreover, Jet bubbling reactor(JBR)is the reactor that fits this technique very well. However, it is difficult to achieve the goal to obtain high enough SO2 absorption efficiency and Mn2+ extraction rate simultaneously in a single JBR. Thereafter, some research work about the effect of additive percentage of pH value buffer solution and oxygen concentration in flue gas on this system of flue gas desulfurization with pyrolusite pulp in a single JBR was carried out, and it was illustrated that the optimized additive percentage of pH value buffer was 30% and 10% when oxygen concentration in flue gas is 21% and 7% respectively. Based on the experiment results, it was proved that under the conditions of simulated flue gas from real flaming coal, if the additive percentage of pH buffer value was 10%, the SO2 absorption efficiency and Mn2+ extraction rate could both reach above 80% in a single JBR. Wherefore, it could be concluded that this technique of flue gas desulfurization is not only operationally but also commercially feasible, and also, promising in industrial application in the future.

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