农业工程学报
農業工程學報
농업공정학보
2014年
5期
57-64
,共8页
于冬冬%倪琦%庄保陆%张宇雷%单建军%管崇武%张成林%吴凡
于鼕鼕%倪琦%莊保陸%張宇雷%單建軍%管崇武%張成林%吳凡
우동동%예기%장보륙%장우뢰%단건군%관숭무%장성림%오범
过滤器%水质%水产养殖%净化%悬浮物%气提式砂滤器%海水循环养殖%水处理
過濾器%水質%水產養殖%淨化%懸浮物%氣提式砂濾器%海水循環養殖%水處理
과려기%수질%수산양식%정화%현부물%기제식사려기%해수순배양식%수처리
filters%water quality%aquaculture%purification%suspended solids%airlift sand filter%marine recirculating aquaculture%water treatment
为解决传统压力式砂滤罐长时间工作后截留大量固体颗粒物而导致的难以反冲洗的问题,该研究在原有设备基础上进行技术改进;研制出了1种可以边工作边反冲洗的气提式砂滤器;气提式砂滤器集过滤、分离、气浮、自动清洗等功能于一体,可以替代传统用于养殖车间的砂滤罐、无阀滤池、微滤机、机械式气浮等物理过滤装置;试验用1~2 mm石英砂作为过滤介质,过滤水以向上流方向从气提式砂滤器底部慢慢上升,污物被石英砂截留,同时,从底部流入定流量气体,使得污物和砂粒同时被提起,最终在顶端的洗砂装置中石英砂被清洗干净并由于重力作用而落回系统,污物和废水从排污口流出;试验表明,气提式砂滤器设备简单、操作简便,不需停机反冲洗,系统运行连续平稳,能耗小并且易于日常维护和检修;数据表明,这种气提式砂滤器对海水循环水养殖系统中的颗粒悬浮物(suspended solids,SS)和化学需氧量(chemical oxygen demand,COD)平均去除率分别为(41.31%±7.72%)、34.04%,同时也降低了氨氮、亚硝酸盐含量,过滤后养殖水颗粒悬浮物质量浓度≤67.33 mg/L。气提式砂滤器在海水循环水养殖系统中进行物理过滤,是1种行之有效的方法,满足了养殖车间的水处理要求。
為解決傳統壓力式砂濾罐長時間工作後截留大量固體顆粒物而導緻的難以反遲洗的問題,該研究在原有設備基礎上進行技術改進;研製齣瞭1種可以邊工作邊反遲洗的氣提式砂濾器;氣提式砂濾器集過濾、分離、氣浮、自動清洗等功能于一體,可以替代傳統用于養殖車間的砂濾罐、無閥濾池、微濾機、機械式氣浮等物理過濾裝置;試驗用1~2 mm石英砂作為過濾介質,過濾水以嚮上流方嚮從氣提式砂濾器底部慢慢上升,汙物被石英砂截留,同時,從底部流入定流量氣體,使得汙物和砂粒同時被提起,最終在頂耑的洗砂裝置中石英砂被清洗榦淨併由于重力作用而落迴繫統,汙物和廢水從排汙口流齣;試驗錶明,氣提式砂濾器設備簡單、操作簡便,不需停機反遲洗,繫統運行連續平穩,能耗小併且易于日常維護和檢脩;數據錶明,這種氣提式砂濾器對海水循環水養殖繫統中的顆粒懸浮物(suspended solids,SS)和化學需氧量(chemical oxygen demand,COD)平均去除率分彆為(41.31%±7.72%)、34.04%,同時也降低瞭氨氮、亞硝痠鹽含量,過濾後養殖水顆粒懸浮物質量濃度≤67.33 mg/L。氣提式砂濾器在海水循環水養殖繫統中進行物理過濾,是1種行之有效的方法,滿足瞭養殖車間的水處理要求。
위해결전통압력식사려관장시간공작후절류대량고체과립물이도치적난이반충세적문제,해연구재원유설비기출상진행기술개진;연제출료1충가이변공작변반충세적기제식사려기;기제식사려기집과려、분리、기부、자동청세등공능우일체,가이체대전통용우양식차간적사려관、무벌려지、미려궤、궤계식기부등물리과려장치;시험용1~2 mm석영사작위과려개질,과려수이향상류방향종기제식사려기저부만만상승,오물피석영사절류,동시,종저부류입정류량기체,사득오물화사립동시피제기,최종재정단적세사장치중석영사피청세간정병유우중력작용이락회계통,오물화폐수종배오구류출;시험표명,기제식사려기설비간단、조작간편,불수정궤반충세,계통운행련속평은,능모소병차역우일상유호화검수;수거표명,저충기제식사려기대해수순배수양식계통중적과립현부물(suspended solids,SS)화화학수양량(chemical oxygen demand,COD)평균거제솔분별위(41.31%±7.72%)、34.04%,동시야강저료안담、아초산염함량,과려후양식수과립현부물질량농도≤67.33 mg/L。기제식사려기재해수순배수양식계통중진행물리과려,시1충행지유효적방법,만족료양식차간적수처리요구。
Traditional pressure sand filter after long time working intercepts large amounts of solid particles and leads to difficult backwash. In order to solve these problems, this study developed an airlift sand filter that can backwash itself while operating by optimizing a traditional filter. The airlift sand filter itself had filtration, separation, flotation, and self-cleaning functions, and could replace the traditional sand filters such as filter cell without valve, mechanical air flotation and other physical filtration device in aquaculture workshop. In the airlift sand filter, quartz sand (in diameter of 1-2 mm) was used as the filter medium, and the aquaculture sewage was flowed upward slowly from the bottom, thus quartz sand could intercept the suspended solids. Meanwhile, the fixed flow gas flowed from the bottom pushed dirt and quartz sand upwards simultaneously. During this process, sand and water were sufficiently contacted with each other. The interaction force between the sand and seawater resulted in production of a large number of bubbles. The suspended solids were then wrapped with the bubbles while quartz sand was cleaned by the sand washing device on the top of the system. The cleaned sand fallen back to the filter system by the gravity, and the suspended solids and waste water flowed out of the outfall. The airlift sand filter has the advantages of simple equipment, convenient operation, backwash without stopping the equipment, smooth and continuous system running, low energy consumption and easy to maintain and repair. The efficiency of the airlift sand filter used for marine recirculating aquaculture systems of the suspended solids (SS) and chemical oxygen demand (COD) was tested. Results showed that removal efficiency of SS and COD by this filter was 41.31%and 34.04%, respectively. Before the filtration, the number of large particles suspended solids (60 μm or higher) was 11.1%, its mass fraction was 71.77% and its mass concentration was 93.53 mg/L. The water processing decreased the number, mass fraction, and mass concentration of the large particles suspended solids to 0.68%, 38.07%, and 15.72 mg/L, respectively. At the beginning of the test, the number of micro particles (60μm or less) was 88.92%, its mass fraction was 28.23%, and its mass concentration was 36.79 mg/L. After the treatment, the micro particles below 30μm accounted for 87.45%, its number of mass fraction was 13.61%, and its mass concentration was 5.62 mg/L. These results suggested that the effect of particulate removal treatment was obvious. Meanwhile, the treatment also reduced the content of ammonia nitrogen and nitrite in the system. After filtration, the suspended solids in recirculating aquaculture systems were≤67.33 mg/L, meeting the requirements of the water treatment in marine recirculating aquaculture workshop by China.