- 更多网络例句与硝化床相关的网络例句 [注:此内容来源于网络,仅供参考]
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The experimental results indicate that nitrate is effectively removed through the autotrophic denitrification process in the sulfur-zeolite fixed bed reactor.
实验结果表明,在硫/沸石固定床反应器内通过自养反硝化作用能使水体中硝酸盐得到有效的去除。
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The active layer in MEEF composed of the granular material from plants, where earthworms act as declogger, decomposer and facilitating a nitrification-denitrification process within the biofilm.
蚯蚓在滤床中起分解和利用污水和污泥中的有机物和营养物质、清通滤床以及促进含氮物质的硝化与反硝化作用。
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Nitrosification and denitrification in an artificial domestic wastewater with low COD were studied in a sequencing batch moving bed biofilm reactor.
在序批式移动床生物膜反应器内,对进水COD较低的条件下,模拟生活污水的亚硝化及脱氮性能进行了研究。
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With retention time prolonged, the concentrations of TN, NH4(superscript +)-N and TP of domestic sewage were obviously reduced in all floating-bed systems, however the NO4(superscript +)-N concentrations were gradualjy accumulated due to the stronger nitrification than denitrification. The plants in floating-bed system increased significantly the N2O flux, which was 174.44μg/(m^2h), 82.19μg/(m^2h), 112. 49μg/(m^2h) and 44.81μg/(m^2h), respectively, for the Lolium mutliflorum, Oenanthe javanica, Vetiveria Zizanioides arid none-plant floating-bed systems.
净化周期内,浮床各系统的TN、NH4-N和TP浓度随着污水停留时间的延长直线下降,而NO3-N浓度却因系统内硝化强度大于反硝化强度而产生了累积;植物的存在明显的促进了浮床系统的N2O排放,浮床黑麦草、水芹、香根草和对照系统N2O的平均排放通量分别为174.44μg/, 82.19μg/, 112.49μg/和44.81μg。
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The feasibility of nitrate removal from nitrified landfill leachate in reactors with different sulfur particle size was studied.
在填充不同粒径硫磺的固定床反应器中,研究脱氮硫杆菌去除垃圾填埋场硝化渗滤污水中硝酸盐的可行性。
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Through carrying on nitrifying potentiality dynamics analysis of the substrate artificial medium in the ecological floating bed, find substrate artificial medium nitrifies approximate to be zero response. the dynamics equation is y =-0.1347x+4.3542, the artificial medium nitrifying potentiality is 3.4×10-5g/h·slice.
通过对生态浮床底层人工介质的反硝化潜力进行动力学分析,发现底层人工介质的反硝化近似为零级反应,动力学方程为y=-0.1347x+4.3542,人工介质反硝化潜力为3.4×10~(-5)g/h·片。
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When A〓-A〓-O-A〓 system, using fixed beds as anaerobic and anoxic reators and draft-tube fluidised bed as aerobic reactor (total hydraulic residence time 26. 2h, 9, 5, 7. 2 and 5h for each stage, and recycle ratio of mixed liquor from oxic reactor to the first anoxic reactor 5: 1), is used, the removal rates of COD, NH〓N and TN reach 97, 95. 5 and 90% respectively (influent COD, NH〓-N and TN 1204. 8, 274. 3 and 443mg/l respectvely).
采用A〓-A〓-O-A〓流程和简捷硝化-反硝化过程,以固定床作厌氧反应器和缺氧反应器,以内循环式生物反应器作好氧反应器,系统总水力停留时间为26.2h,各段停留时间分别为9h,5h,7.2h和5h,好氧反应器和第一级缺氧反应器之间的混合液回流比为5:1,系统进水COD为1204.8mg/l,NH〓-N为274.3mg/l,TN为443mg/l时,COD、NH〓-N和TN的去除率分别可达97%、95.5%和90%。
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To study the flow pattern and construct the flow model, the tracer tests were performed using pulse stimulus-response technique .
采用脉冲刺激响应技术,对稳态内循环颗粒污泥床硝化反应器进行了示踪试验。
- 更多网络解释与硝化床相关的网络解释 [注:此内容来源于网络,仅供参考]
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skimmer:撇渣器
3.全生态处理:顾名思义是以硝化菌着床作生化处理的方式,这种处理方式以欧洲较多,需要有较复杂的生态循环设计,对迎风面的撇渣器(Skimmer)设置,考验景观设计师对绿色循环系统的配置能力;池水净化的过程是以水生植物的根茎吸收和过滤水中的污染物质,
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nitriary:硝化床
nitriacidiumion 硝酸合氢离子 | nitriary 硝化床 | nitric 硝石的 氮的