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作 者:黄承武[1] 李树猷[1] 傅玉治[2] 张淑兰[2] 韩树青[2] 刘连惠[3] 赵之相 鲍瑞才 张方权
机构地区:[1]中国预防医学科学院环境卫生与卫生工程研究所 [2]天津市卫生防病中心 [3]廊坊市环境保护设备厂 [4]廊坊地区卫生防疫站 [5]天津市塘沽区地方病防治办公室
出 处:《中国公共卫生学报》1990年第2期65-68,共4页
摘 要:本文研究了饮水除氟及含氟废水处理新工艺。用0.1M硫酸注入原水使其pH由8.4降至6.0~6.5,再通过一个充填粒径为0.45~1.2或2mm的活性氧化铝滤罐。出水的平均氟化物水平均0.5mg/L,但这种水可与适当体积的原水混合,使供饮用的处理水氟化物水平调整到0.90~0.95mg/L。本工艺使滤料的除氟容量由通常可接受的1.2提高到4.5mg F^-/g Al_2O_3以上。每立米水处理费(包括化学品、滤料补充、电力和人工)为0.10元,与传统工艺(不调原水pH的为0.29元/m^3处理水)相比,节省了66%。活性氧化铝再生用0.80~0.85%氢氧化钠溶液使滤料的溶解降到最低程度,强碱性含氟废水经中和及化学沉淀后得到了处理。This paper studies a new technology of water defluoridation and fluoride waste treatment. The pH of raw water is lowered from 8.4 to 6.0—6.5 by 0.1M sulfuric acid injection, then filtered through a vessel filled with activated alumina (φ:0.45—1.2, or 2mm). Average fluoride level of effluent is about 0.5mg/L, however this water can be blended by suitable volume of raw water, the fluoride level of treated water is adjusted into the range of 0.90—0.95mg/L. This technology increased the fluoride removal capacity of bed material from the generally accepted level of 1.2 to more than 4.5mg F^-/g Al_2O_3. The operating cost of this technology including chemicals, activated alumina replacement, electricity and labor is ¥ 0.10/m^3 of treated water has saved by 66% as compared with the conventional technology (¥0.29/m^3 of treated water for raw water without pH adjustment). The regeneration of activated alumina employs 0.80—0.85% sodium hydroxide solution to minimize media dissolving. Caustic fluoride waste is treated by neutralization and chemical precipitation.
分 类 号:R123.6[医药卫生—环境卫生学]
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