1) low strength organic wastewater
低浓度有机废水
1.
Influence of temperature on UASB reactor treating low strength organic wastewater;
温度对UASB反应器处理低浓度有机废水的影响
2) low concentration organic wastewater
低浓度有机废水
1.
Experimental study on start-up of low concentration organic wastewater treatment in IC reactor;
IC反应器处理低浓度有机废水的启动实验研究
3) organic wastewater with medium-low concentration
中低浓度有机废水
1.
Application of ETTS to the treatment of organic wastewater with medium-low concentration;
ETTS在中低浓度有机废水处理中的应用
4) high concentration organic wastewater
高浓度有机废水
1.
Operation property of UASB reactor in treatment of high concentration organic wastewater at low temperature;
低温下UASB反应器处理高浓度有机废水的运行特性研究
2.
Study on the function of the integrated two phase anaerobic reactor used in the high concentration organic wastewater treatment;
一体化两相厌氧反应器处理高浓度有机废水的性能研究
3.
Treatment of high concentration organic wastewater by chemical complexation extraction;
络合萃取法处理高浓度有机废水
5) high strength organic wastewater
高浓度有机废水
1.
Set-up of EGSB reactor in treatment of high strength organic wastewater and microbiofacies thereof;
EGSB处理高浓度有机废水的启动与微生物相
2.
A pilot-scale study of high strength organic wastewater treatment using anaerobic digestion-ultrafiltration process;
高浓度有机废水厌氧膜生物工艺处理的中试研究
3.
The change law of organic loading in the course of high strength organic wastewater treatment by expanded granular sludge bed (EGSB) was studied.
研究了厌氧颗粒污泥膨胀床(EGSB)反应器处理高浓度有机废水过程中的有机负荷变化规律。
6) high-strength organic wastewater
高浓度有机废水
1.
Study on ABR treating high-strength organic wastewater;
厌氧折流板反应器处理高浓度有机废水
2.
An experiment on the EGSB reactor,which treats high-strength organic wastewater,was implemented for 83 days at ambient temperature.
EGSB反应器在环境温度下运行83 d的结果表明,当水温为14~29℃时,处理高浓度有机废水的EGSB在不加热的情况下运行良好。
3.
A lab-scale continuous experiment was designed to investigate the effect of influent COD concentrations((11?000),(15?000),(30?000)(mg/L))or hydraulic retention time(HRT 42,25 h)on the microareobic treatment performance of simulated high-strength organic wastewater.
考察改变进水COD浓度(11000、15000、30000 mg/L)或水力停留时间(HRT为42 h、25 h)对模拟高浓度有机废水微好氧连续小试处理效果的影响,并采用荧光原位杂交-流式细胞术(FISH-FCM)、聚合酶链式反应-变性梯度凝胶电泳(PCR-DGGE)等分子生物学技术及Biolog FF微孔板法分析了不同处理阶段稳定期曝气柱污泥的微生态变化,以探讨进水COD浓度或HRT改变时微好氧处理效果变化的微生态机制。
补充资料：焦化厂含酚氰废水处理设计(见含酚氰废水处理设计)
焦化厂含酚氰废水处理设计(见含酚氰废水处理设计)
design of phenolic and cyanic waste water treatment for coking plant
J iaohuaehang honfenging feishui ehuli sheji焦化厂含酚氛废水处理设计(design of phe-nolie and eyanie waste water treatment foreoking plant)见含酚氛度水处理设计。
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