1) anoxic-anaerobic-aerobic system
倒置AAO工艺
1.
Material and energy flow of activated sludge in anoxic-anaerobic-aerobic system;
倒置AAO工艺中物料及能量流向的研究
2) reverse A/A/O new process
倒置AAO新工艺
3) AAO process
AAO工艺
1.
Fully coupled activated sludge model (FCASM3) Part 3:Numerical simulation of AAO process for optimum operating conditions;
全耦合活性污泥模型(FCASM3)Ⅲ:AAO工艺最佳运行工况数值模拟
2.
Pe (Peclet number) effects for wastewater treatment of Deqing Shishan WWTP′s AAO process were studied using the validated Biological-Hydraulic coupled model (FCASM3-Hydro) based on the Fully Coupled Activated Sludge Model 3 (FCASM3).
利用校验完成的生物场-水力场耦合模型(FCASM3-Hydro)以及生物场-水力场-温度场耦合模型(FCASM3-Hydro-Temp)对德清县狮山污水处理厂的AAO工艺系统进行模拟,分别考察反应池Pe准数值以及温度对污水处理效果的影响。
3.
Local experiments for Biological-Hydraulic-Temperature coupled model validation were carried out in the Deqing Shishan WWTP with an AAO process.
以采用AAO工艺的德清县狮山污水处理厂作为生物场-水力场-温度场耦合模型校验的现场试验基地。
4) Reversed A/A/O process
倒置A/A/O工艺
1.
On the base of analysis of wastewater treatment plant original process operation status and the basic principle of biological nitrogen and phosphorus removal process,the existing problems were discussed in the original process(A/A/O) and more mature biological nitrogen and phosphorus removal process including modified A/A/O,UCT,MUCT and reversed A/A/O process.
根据污水厂原有工艺(A/A/O)的运行状况和生物脱氮除磷的基本原理,对水厂的原有工艺(A/A/O)和较成熟的生物脱氮除磷改良A/A/O工艺、UCT、MUCT和倒置A/A/O工艺现存问题进行了分析,从而指出污水厂扩建工程中选择倒置A/A/O工艺的必要性。
5) time sequence AAO new process
时序AAO新工艺
6) simultaneous AAO new process
同步AAO新工艺
补充资料：AAO
分子式：C2H5NO
分子量：59.07
CAS号：107-29-9
性质：密度0.969。熔点44-46°C。沸点115°C。折射率1.425-1.127。闪点38°C。水溶性soluble。
分子量：59.07
CAS号：107-29-9
性质：密度0.969。熔点44-46°C。沸点115°C。折射率1.425-1.127。闪点38°C。水溶性soluble。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条