Zhong Zhaoping, Jin Baosheng, Huang Yaji, Zhou Hongcang, Lan Jixiang
Department of Power Engineering, Research Institute of Thermal Energy Engineering, The Key Laboratory of Clean Coal Power Generation and Combustion Technology of Ministry of Education, Southeast University, Nanjing 210096, PR China.
Waste Manag. 2006;26(6):580-6. doi: 10.1016/j.wasman.2005.06.002. Epub 2005 Jul 28.
This paper describes the experimental study of dioxins removal from flue gas from a co-combustion municipal solid waste and coal incinerator by means of a fluidized absorption tower and a fabric filter. A test rig has been set up. The flow rate of flue gas of the test rig is 150-2000 m3/h. The system was composed of a humidification and cooling system, an absorption tower, a demister, a slurry make-up tank, a desilter, a fabric filter and a measurement system. The total height of the absorption tower was 6.5m, and the diameter of the reactor pool was 1.2 m. When the absorbent was 1% limestone slurry, the recirculation ratio was 3, the jet rate was 5-15 m/s and the submerged depth of the bubbling pipe under the slurry was 0.14 m, the removal efficiency for dioxins was 99.35%. The concentration of dioxins in the treated flue gas was 0.1573 x 10(-13)kg/Nm3 and the concentration of oxygen was 11%. This concentration is comparable to the emission standards of other developed countries.
本文描述了通过流化吸收塔和织物过滤器从城市固体废物与煤共燃焚烧炉的烟气中去除二噁英的实验研究。搭建了一个试验台。试验台的烟气流速为150 - 2000立方米/小时。该系统由加湿冷却系统、吸收塔、除雾器、浆液补充罐、除泥器、织物过滤器和测量系统组成。吸收塔总高度为6.5米,反应池直径为1.2米。当吸收剂为1%的石灰石浆液、循环比为3、喷射速率为5 - 15米/秒且鼓泡管在浆液下的浸没深度为0.14米时,二噁英的去除效率为99.35%。处理后烟气中二噁英的浓度为0.1573×10(-13)千克/标准立方米,氧气浓度为11%。该浓度与其他发达国家的排放标准相当。