Zhai Shang-peng, Liu Jing, Xin Chang-xia, Tang Song-song, Zhang Peng, Xiao You-guo, Ma Zheng-fei
Shanghai Clear Environmental Protection Science and Technology Co. Ltd., Shanghai 201203, China.
Huan Jing Ke Xue. 2006 May;27(5):850-4.
A developed flue gas desulfurization and dust removal process with a cross-flow moving bed filled with activated coke (AC) was tested on a pilot scale with the gas treatment capacity of 1000 mg x h(-t). The results show that a easy-operating and stable-running pilot-scale testing equipment can be reached, and under the conditions of testing space velocity, the feed gas temperature of 120 degrees C, SO2 concentrations of 3232-6006 mg x m(-3) and dust concentration of 89.3-1599.7 mg x m(-3), the high efficiency of flue gas desulfurization and dust removal is reached with the purity of dust less than 50 mg x m(-3). In the technology, the spent AC was regenerated by heating, and the SO2 concentration in the desorption gas is about 40.1%, which can be efficiently recovered as a sulfur resource. Favorable economy benefit can be reached by using the process.
在中试规模下对一种采用填充活性焦(AC)的错流移动床的成熟烟气脱硫除尘工艺进行了测试,气体处理能力为1000 mg·h⁻¹。结果表明,可以实现操作简便且运行稳定的中试规模测试设备,并且在测试空速、进料气体温度为120℃、SO₂浓度为3232 - 6006 mg·m⁻³以及粉尘浓度为89.3 - 1599.7 mg·m⁻³的条件下,可实现高效的烟气脱硫除尘,粉尘纯度低于50 mg·m⁻³。在该技术中,废活性焦通过加热进行再生,解吸气中的SO₂浓度约为40.1%,可作为硫资源有效回收。采用该工艺可获得良好的经济效益。