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1)  temporal aeration
瞬间曝气
2)  instantaneous aeration
瞬时曝气
3)  instantaneous aerator
瞬时曝气器
4)  intermittent aeration
间歇曝气
1.
Effects of nutritional conditions and intermittent aeration on accumulation of PHB in activated sludge;
营养条件与间歇曝气方式对活性污泥累积聚-3-羟基丁酸酯的影响
2.
Study on nitrogen and phosphorus removal from domestic sewage in oxidation ditch with intermittent aeration;
连续流间歇曝气氧化沟处理生活污水脱氮除磷研究
3.
A View on the Prospect of Continuous Flow-intermittent Aeration Process and Its Development;
连续进出水间歇曝气工艺发展展望
5)  aeration time
曝气时间
1.
On the basis of domastic sewage treatment plant design, it is discussed that the influencl of aeration time on the effeat of CAST craft.
结合姜堰市城市生活污水处理厂的设计,在CAST工艺中,进行了曝气时间对COD和NH3-N去除率影响的探讨。
2.
Microaerobic biological technology was used for methanol wastewater treatment through a lab-scale experiment at room temperature,the relationships of removal efficiency of COD with influent COD,aeration quantity and aeration time were discussed.
在常温条件下进行微氧生物处理高浓度甲醇废水实验,研究COD去除率与进水COD浓度、曝气量和曝气时间的关系,在实验中最佳的水平搭配为:进水COD质量浓度2500 mg/L,曝气量90 L/h,曝气时间11 h,与回归分析所得出的最佳工艺条件相吻合,最后通过响应曲面等高线分析得出常温下甲醇废水微氧生物处理的适宜范围。
3.
The best aeration time and the best pH value were measured, and the sludge volume rate and contamination tolerance load were tested experimentally.
实验测定了污泥沉降性能,测试了最佳曝气时间、最佳pH值范围以及SBR处理系统耐污染的负荷。
6)  aeration on/off time
曝气/停曝时间
1.
The influence of the dissolved oxygen(DO) concentration and aeration on/off time on short-cut nitrification and denitrification were investigated.
本试验将反应器温度控制在30℃左右,采用间歇曝气的运行方式,研究了溶解氧浓度及间歇曝气/停曝时间对SMBR实现短程硝化反硝化脱氮的影响,同时研究了胞外聚合物各组分对膜污染状况的影响。
2.
To improve the total nitrogen (TN) removal efficiency of membrane bioreactor(MBR), dissolved oxygen (DO) and aeration on/off time were controlled to study the possibility of total nitrogen removal through short-cut nitrification and denitrification.
为了改善膜生物反应器(MBR)的脱氮效果,考察了不同溶解氧浓度(DO)、曝气/停曝时间对MBR工艺实现短程硝化反硝化生物脱氮的可能性以及对膜污染的影响。
补充资料:变量曝气法
分子式:
CAS号:

性质:又称变量曝气(法)。是废水活性污泥法的一种改良型。为适应曝气池进水口至出水口之间混合液中有机负荷不同的需要,对曝气池的不同部分供给不同空气量,入口处供给空气量较多,出口附近则较少,使得空气量与混合液的需氧量大致成正比。此法可节省供氧量,不需设置初次沉淀池。

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