中国给水排水
中國給水排水
중국급수배수
CHINA WATER & WASTEWATER
2009年
23期
79-81
,共3页
螺旋升流塔式光催化反应器%离心%水力停留时间%回收率
螺鏇升流塔式光催化反應器%離心%水力停留時間%迴收率
라선승류탑식광최화반응기%리심%수력정류시간%회수솔
spiral up-flow tower-type photocatalysis reactor%centrifugation%hydraulic retention time%recovery rate
采用颗粒污染物的旋流分离模型设计了螺旋升流塔式光催化反应器,能够在悬浮态光催化反应系统中提高光催化剂的回收率.反应器采用塔式结构布置,能有效提高反应器的光照面积与反应液体积之比(A/V值),在本试验条件下A/V值可达到12.95.采用该反应器处理硝基苯模拟废水,当硝基苯初始浓度为466 mg/L时,反应器对硝基苯的去除率稳定在60%左右,运行12 h后对光催化剂的回收率为92.80%.
採用顆粒汙染物的鏇流分離模型設計瞭螺鏇升流塔式光催化反應器,能夠在懸浮態光催化反應繫統中提高光催化劑的迴收率.反應器採用塔式結構佈置,能有效提高反應器的光照麵積與反應液體積之比(A/V值),在本試驗條件下A/V值可達到12.95.採用該反應器處理硝基苯模擬廢水,噹硝基苯初始濃度為466 mg/L時,反應器對硝基苯的去除率穩定在60%左右,運行12 h後對光催化劑的迴收率為92.80%.
채용과립오염물적선류분리모형설계료라선승류탑식광최화반응기,능구재현부태광최화반응계통중제고광최화제적회수솔.반응기채용탑식결구포치,능유효제고반응기적광조면적여반응액체적지비(A/V치),재본시험조건하A/V치가체도12.95.채용해반응기처리초기분모의폐수,당초기분초시농도위466 mg/L시,반응기대초기분적거제솔은정재60%좌우,운행12 h후대광최화제적회수솔위92.80%.
Based on the cyclone separator model for granular pollutants, a spiral up-flow tower-type photocatalysis reactor was designed to increase the recovery rate of photocatalyst. In order to reach a high A/V ratio (the ratio of illumination area to reaction solution volume), a tower structure was used on this reactor, and the A/V ratio can reach 12.95 in this experimental condition. This reactor was used to treat the nitrobenzene simulated wastewater. When the initial concentration of nitrobenzene is 466 mg/L, the removal rate of nitrobenzene is about 60%, and the photocatalyst recovery rate reaches 92.80% after 12h.