工厂化循环水养殖中臭氧/紫外线反应系统的水处理性能

为增强臭氧在水产应用的安全性,满足工厂化循环水养殖对有机物去除和水体消毒的需要,该文开发O3/UV反应系统。通过试验方法研究该系统臭氧投加溶解区适宜的臭氧投加流量和处理量的关系、紫外辐射剂量配比等工艺参数,及对水质净化效果和水体消毒灭菌效果的影响等。试验结果表明:1)在满足所需水中溶解臭氧浓度的条件下,采用较低臭氧进气流量和较高进水流量有利于提高系统的臭氧溶解率和利用率。该系统在水流量为5 m3/h,臭氧投加量为(8.78±0.60)g/h时可得到水中臭氧溶解质量浓度为1.53 mg/L的臭氧水,臭氧溶解率为82.7%,臭氧利用率为97.7%。2)增加紫外灯的功率和数量均可提高对臭氧的去除率,...

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Published in农业工程学报 Vol. 30; no. 23; pp. 253 - 259
Main Author 管崇武 杨菁 单建军 张海耿 刘晃 王欣
Format Journal Article
LanguageChinese
Published 农业部渔业装备与工程技术重点实验室,中国水产科学研究院渔业机械仪器研究所,上海 200092 2014
上海理工大学医疗器械与食品学院,上海 200093%农业部渔业装备与工程技术重点实验室,中国水产科学研究院渔业机械仪器研究所,上海 200092%上海理工大学医疗器械与食品学院,上海,200093
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ISSN1002-6819
DOI10.3969/j.issn.1002-6819.2014.23.032

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Summary:为增强臭氧在水产应用的安全性,满足工厂化循环水养殖对有机物去除和水体消毒的需要,该文开发O3/UV反应系统。通过试验方法研究该系统臭氧投加溶解区适宜的臭氧投加流量和处理量的关系、紫外辐射剂量配比等工艺参数,及对水质净化效果和水体消毒灭菌效果的影响等。试验结果表明:1)在满足所需水中溶解臭氧浓度的条件下,采用较低臭氧进气流量和较高进水流量有利于提高系统的臭氧溶解率和利用率。该系统在水流量为5 m3/h,臭氧投加量为(8.78±0.60)g/h时可得到水中臭氧溶解质量浓度为1.53 mg/L的臭氧水,臭氧溶解率为82.7%,臭氧利用率为97.7%。2)增加紫外灯的功率和数量均可提高对臭氧的去除率,但增加紫外灯的数量对其性能提升效果更明显。该系统在紫外剂量为1 996 MJ/cm2,对残留臭氧的去除率为83.82%。3)该系统对紫外消光度、总有机碳、水色等指标的去除率相比单独使用臭氧分别提升109.95%、89.77%和51.44%,杀菌率可达97%以上,实现工厂化循环水养殖低臭氧残留条件下的有机物有效去除和消毒杀菌。
Bibliography:11-2047/S
Guan Chongwu, Yang Jing, Shan Jianjun, Zhang Haigeng, Liu Huang, Wang Xin (1. Key laboratory of Fishery Equipment and Engineering, Ministry of Agriculture, Fishery Machinery and Instrument Research Institute, Chinese Academy of Fishery Sciences, Shanghai 200092, China; 2. School of Medical Instrument and Food Engineering, University of Shanghai for Science and Technology, Shanghai 200093, China)
water treatment; wastewater; ozone; O3/UV reaction system; advanced oxidation technologies; organic matter removal; disinfection sterilization; recirculating aquaculture systems
In order to improve the water treatment performance of ozone in recirculating aquaculture systems, and enhance its application safety in the field of aquaculture, the O3/UV integration reaction system were designed. The reaction system was mainly composed of ozone addition dissolved area, ultraviolet catalytic reaction area, stay reaction area. The system was 1 250 mm of high, 750 mm in diameter, and the ultraviolet catalytic reaction w
ISSN:1002-6819
DOI:10.3969/j.issn.1002-6819.2014.23.032