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   焦化废水 的翻译结果: 查询用时:0.671秒
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焦化废水     
相关语句
  coking wastewater
     Research on the COD Removing Characteristic of the A_1-A_2 Section with A_1-A_2-O-M Technique from Coking Wastewater
     焦化废水A_1-A_2-O-M工艺A_1-A_2段COD去除特性研究
短句来源
     Research on Treatment of Nonbiodegradable and Toxic Organic Substances in Coking Wastewater with UV+F_e~(2+)+H_2O_2
     UV+F_e~(2+)+H_2O_2处理焦化废水中难生物降解的有机毒物的研究
短句来源
     A~2/O Process for the Treatment of Coking Wastewater
     A~2/O工艺处理焦化废水
短句来源
     Research on the Treatment of Coking Wastewater in A1-A2-O-M System
     A_1-A_2-O-M工艺处理焦化废水的实验研究
短句来源
     A~2/O process for treating coking wastewater
     A~2/O法处理焦化废水
短句来源
更多       
  coke plant wastewater
     Study on the A_1-A_2 Stage in Coke Plant Wastewater Treatment by A_1-A_2-O_1-O_2 Technology
     A_1-A_2-O_1-O_2工艺A_1-A_2段处理焦化废水试验研究
短句来源
     The Test Research of Coke Plant Wastewater Biological Treatment by the A_1 and A_2 Stage of A_1-A_2-O-M Process
     焦化废水A_1-A_2-O-M工艺A_1-A_2段生物处理试验研究
短句来源
     Research of Aerobic Stages Biological Treatment of Coke Plant Wastewater by A_1-A_2-O_1-O_2
     A_1-A_2-O_1-O_2工艺好氧段处理焦化废水试验研究
短句来源
     After the treatment by adsorption catalytic oxidation process,the COD of coke plant wastewater is reduced to 43.2 mg/L from 1 173.0 mg/L,and the removal efficiency of COD is up to 96.3%.
     经活性炭吸附 - Fenton试剂催化氧化处理后 ,焦化废水的COD从 1 1 73mg/ L 降至 4 3.2 m g/ L,去除率达 96 .3%。
短句来源
     Research of O-M Biological Treatment of Coke Plant Wastewater by A~2-O-M
     焦化废水A~2-O-M工艺O-M段生物处理试验研究
短句来源
更多       
  coking waste water
     Research on the COD Removing Characteristic of the A_1-A_2 Section with A_1-A_2-O-M Technique from Coking Wastewater
     焦化废水A_1-A_2-O-M工艺A_1-A_2段COD去除特性研究
短句来源
     Research on Treatment of Nonbiodegradable and Toxic Organic Substances in Coking Wastewater with UV+F_e~(2+)+H_2O_2
     UV+F_e~(2+)+H_2O_2处理焦化废水中难生物降解的有机毒物的研究
短句来源
     A~2/O Process for the Treatment of Coking Wastewater
     A~2/O工艺处理焦化废水
短句来源
     Research on the Treatment of Coking Wastewater in A1-A2-O-M System
     A_1-A_2-O-M工艺处理焦化废水的实验研究
短句来源
     A~2/O process for treating coking wastewater
     A~2/O法处理焦化废水
短句来源
更多       
  coke-plant wastewater
     The results show that A1-A2/O system is more efficient than A2/O system for the coke-plant wastewater, the average effluent COD and NH3-N of A1-A2/O system is lower than that of A2/O system about 10~30mg/l and 25. 8mg/l;
     结果表明:A_1-A_2/O系统处理焦化废水的效果优于A_2/O系统,出水COD和NH_3—N平均低10~30mg/L和25.8mg/L;
短句来源
     A COMPARISON STUDY BETWEEN A_1-A_2/OAND A_2/O FIXED BIOFILM SYSTEMS ON THE COKE-PLANT WASTEWATER TREATMENT
     A_1-A_2/O与A_2/O系统处理焦化废水的比较研究
短句来源
     Study on the technical parameters of coke-plant wastewater treatment by the A~2/O biofilm system
     A~2/O生物膜系统处理焦化废水工艺参数研究
短句来源
     A test to compare A1-A2/O (Anaerobic-Anoxic/Oxic) and A2/O (Anox-ic/Oxic) fixed-biofilm System has been running for coke-plant wastewater under the same operation conditions.
     在相同运行条件下,进行了A_1-A_2/O(厌氧-缺氧/好氧)与A_2/O(缺氧/好氧)固定床处理焦化废水的比较试验.
短句来源
     COKE-PLANT WASTEWATER TREATMENT WITH A-A/0 SYSTEM IN A PILOT PLANT
     A-A/O法处理焦化废水中试研究
短句来源
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  coking wastewater
The seed sludge was obtained from a local coal-coking wastewater treatment facility and was acclimated in the laboratory.
      
Cloning of Environmental Genomic Fragments as Physical Markers for Monitoring Microbial Populations in Coking Wastewater Treatme
      
A laboratory-scale anaerobic-anoxic-oxic fixed biofilm system treating coking wastewater was operated with (LR mode) or without effluent recirculation (LNR mode).
      
  coke-plant wastewater
Catalytic Wet Air Oxidation of Coke-Plant Wastewater on Ruthenium-Based Eggshell Catalysts in a Bubbling Bed Reactor
      
Catalytic wet air of coke-plant wastewater was studied in a bubbling bed reactor.
      
The high activity of eggshell catalyst for treatment of coke-plant wastewater can be attributed to the higher density of active Ru sites in the shell layer than that of the corresponding uniform catalyst with the same Ru loading.
      
It has been also evidenced that the active Ru sites in the internal core of uniform catalyst have very little or no contribution to CODcr and NH3-N removal in the total oxidation of coke-plant wastewater.
      
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