采用计算流体动力学软件Fluent对袋式除尘器内部流场进行三维数值模拟,提出3种优化灰斗结构模型,得到除尘器灰斗内部的气流流场分布特征,将其与原灰斗结构的气流分配效果对比. 结果表明,原灰斗结构气流进入灰斗后形成一股冲击射流,在选取的监测面上速度最大为8.3 m/s,最小仅为0.5 m/s,速度分布均方根值高达0.99,速度在监测面上分布极不均匀;3种优化结构中袋室内气流均匀性均比原灰斗结构显著改善,在灰斗内添加导流装置可提高气流分配的均匀性;3种优化结构中,添加竖直导流板的灰斗结构对改善气流分配均匀性最明显,比原灰斗结构流动均匀性提高了41.41%,而考虑射流偏转添加倾斜导流板或翼板的优化结构与竖直导流板相比流动均匀性无显著变化,灰斗内部射流偏转对流场分布的影响可忽略.
The computational fluid dynamic simulation of the airflow inside a bag filter was carried out, three optimized structures of the hopper were proposed to improve the original hopper structure. The flow characteristics of the airflow inside the bag filter were obtained. The effect of airflow distribution of three optimized structures were compared with original structure. The results showed that the airflow in the hopper of the original structure formed an impinging jet. The maximum velocity was 8.3 m/s, and the minimum velocity was only 0.5 m/s, the relative root mean square velocity of the monitoring surface was 0.99. The velocity distribution on the corresponding monitoring surface was extremely uneven along the mainstream direction. The airflow uniformity inside the bag filter was improved in all three optimized structures, thus it was possible to improve the airflow uniform distribution by adding baffles. Considering the airflow uniform distribution inside the bag filter, adding vertical baffles was optimal, which can be improved by 41.41%. However the uniformity of the optimized structures with the third tilted baffle or the straight plate with a wing were not significantly improved compared to the addition of vertical baffles. Therefore when the hopper structure is optimized, the influence of the deflection of impinging jet on the airflow distribution inside the hopper can be neglected.
[1]朱法华.袋式除尘技术的发展及其在燃煤电厂烟气处理中的应用[J].中国电力, 2002, 35(8):56-60
[2]高晖, 郭烈锦.除尘器袋室结构改进及内部气固两相流动特征分析[J].西安交通大学学报, 2000, 34(5):50-54
[3]Thomas Wilis Candido Pereira, Felipe Bezerra Marques, et al. The influence of the fabric filter layout of in a flow mass filtrate[J].Journal of Cleaner Production, 2016, 2016(111):117-124
[4]李少华, 宋阳, 王铁营, 王艳鹏.下进风袋式除尘器内部流场的数值模拟[J].东北电力大学学报, 2015, 35(1):12-17
[5]高广德, 何璐璐.导流板对袋式除尘器流场影响的数值分析[J].煤矿机械, 2010, 31(12):38-40
[6]Chi-Jen Chen, Man-Ting Cheng.Effect of flow distributors on uniformity of velocity profile in a baghouse[J].Journal of the Air & Waste Management Association, 2005, 55(7):886-892
[7]周睿, 沈恒根.电解铝用袋式除尘器气流流动规律的模拟研究[J].建筑热能通风空调, 2013, 32(6):86-90
[8]柴旭昇.袋式除尘器气流均匀性及优化的数值模拟研究[D]. 湖南: 南华大学, 2015.
[9]毛锐, 刘根凡, 邓翔, 樊宁.布袋除尘器结构改进的数值模拟研究[J].环境工程, 2015, 2015(3):77-81
[10]潘伶, 杨燕珍.袋式除尘器内部流场的数值模拟[J].环境工程学报, 2012, 6(8):2750-2754
[11]党小庆, 袁胜利, 姚群, 等.直通式袋式除尘器流量分配计算流体动力学方法研究[J].热力发电, 2005, 2005(9):29-32
[12]王福军.计算流体动力学分析——CFD软件原理与应用[M]. 北京: 清华大学出版社, 2004.
[13]单光圣, 刘旭, 陈新刚, 林海青.袋式除尘器设计要点[J].冶金能源, 2008, 27(4):10-19
[14]张相亮, 沈恒根, 周睿等.袋式除尘器进气均布板结构参数对气流分布的影响分析[J].环境工程学报, 2012, 30(4):76-79
[15]付海明, 赵友军.袋式除尘器流场动态测试及优化[J].中南大学学报, 2010, 41(2):799-806
[16]宁波, 王作杰, 张松, 魏林生.入口管道对袋式除尘器性能影响因素研究[J].安全与环境学报, 2013, 13(6):58-62
[17]汪家琼, 刘根凡, 邓翔.软件在布袋除尘器挡板和导流板设计中的应用[J].石油化工设备, 2008, 37(5):71-73