Zhang Guilin, Song Shulei, Guo Junwei, Zhang Bo
School of Mechanical and Electronic Engineering, Suzhou University, Suzhou, Anhui 234000, China.
Key Laboratory of Coal Processing and Efficient Utilization of Ministry of Education, China University of Mining & Technology, Xuzhou, Jiangsu 221116, China.
ACS Omega. 2022 Jan 21;7(4):3804-3811. doi: 10.1021/acsomega.1c06736. eCollection 2022 Feb 1.
A gas-solid separation fluidized bed, which belongs to dry separation and can save a lot of water resources, is an important method for coal quality improvement. The effect of regional blockage of the air distributor on the fluidization effect was investigated by varying the blockage area and fluidization gas velocity, and the influence law of blockage of an air distributor on bed stability was revealed. In this paper, the micro-differential pressure sensor is used as a testing tool to analyze the regional characteristics of the fluidized bed blockage hole. The results show that when the air distributor is plugged, the standard deviations of the pressure fluctuation are largest at a height of 100 mm, all reaching more than 2.0, and that the pressure fluctuation at the bottom is greater than that at the top. When the plugged area fraction increases from 1/8 to 1/2, the density fluctuation range at the bottom of the plugged area decreases from 0.2 to 0.04 g/cm, while the range of influence increases from 10 to 16 cm axially. With the increase of fluidization gas velocity, the mixing effect of particles is improved to an extent, and the range of the affected zone is gradually reduced.
气固分离流化床属于干法分离,可节约大量水资源,是改善煤炭质量的重要方法。通过改变堵塞面积和流化气体速度,研究了空气分布器区域堵塞对流化效果的影响,揭示了空气分布器堵塞对床层稳定性的影响规律。本文采用微差压传感器作为测试工具,分析流化床堵塞孔的区域特性。结果表明,当空气分布器堵塞时,压力波动的标准差在100mm高度处最大,均达到2.0以上,且底部压力波动大于顶部。当堵塞面积分数从1/8增加到1/2时,堵塞区域底部的密度波动范围从0.2g/cm减小到0.04g/cm,而轴向影响范围从10cm增加到16cm。随着流化气体速度的增加,颗粒的混合效果得到一定程度的改善,影响区域范围逐渐减小。