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煤砂双层滤料滤池气水反冲洗参数探究及应用

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为解决济阳某10万m3/d水厂煤砂双层滤料滤池反冲洗不彻底、滤料流失、混层等问题,对滤池进行了水反冲流体力学(CFD)模拟,指导水冲阶段反冲洗强度的选取,并在现场进行了中试试验。试验结果表明:采用气水反冲洗模式,当气冲阶段 qs=17。0 L/(m2·s)、t=3 min 时;水冲阶段,梯度提升水冲强度,在 qw1=4。5 L/(m2·s)、t1=2 min,qw2=7。0 L/(m2·s)、t2=3 min,qw3=17。5 L/(m2·s)、t3=3 min时,反冲洗后滤料含泥量可控制在0。1%以下,并可恢复滤料混层。将最优参数在工程现场应用后,有效解决水厂反冲洗问题,延长过滤周期,滤池反冲洗年耗水量减少192 720 m3。
Exploration and Application of Gas-Water Backwashing Parameters in Anthracite-Sand Double-Layer Filter
In order to solve the problems of incomplete backwashing,loss of filter material and mixed layer in a 100 000 m3/d water treatment plant(WTP)in Jiyang City,the water backwash fluid dynamics(CFD)simulation of the filter was carried out to guide the selection of backwash strength in the water flushing stage,and pilot tests were carried out in the field.The test results showed that the gas-water combined recoil mode was adopted,with an air flushing phase of qs=17.0 L/(m2·s)and t=3 min,and during the water flushing phase,gradually increasing water flushing intensity with qw1=4.5 L/(m2·s)and t1=2 min,qw2=7.0 L/(m2·s)and t2=3 min,and qw3=17.5 L/(m2·s)and t3=3 min,the mud content of the filter material could be controlled below 0.1%and the mixed layer of the filter material could be restored.After the application of the optimal parameters in the project site,the backwashing problem of the WTP could be effectively solved.The filtration period could be extended,and the water consumption of the filter tank could be reduced by 192 720 m3.

anthracite-sand double-layer filterCFD simulationgas-water backwashingmud contentmixed-layer

张欢、刘霄鹏、王栋、谷雷严、杨建华、冯文

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中国城市建设研究院有限公司,北京 100120

潍坊市自来水有限公司,山东潍坊 261000

济阳水务发展有限公司,山东济南 251400

聊城水务集团有限公司,山东聊城 252000

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煤砂双层滤料滤池 CFD模拟 气水反冲洗 含泥量 混层

中国建设科技集团科技创新基金青年科技基金

Z2022Q14

2024

净水技术
上海市净水技术学会,上海市城乡建设和交通委员会科学技术委员会办公室

净水技术

CSTPCD
影响因子:0.643
ISSN:1009-0177
年,卷(期):2024.43(3)
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