西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Advanced Treatment

Advanced Treatment in Activated Sludge Process
Advanced Treatment in Activated Sludge Process

Activated sludge process Aeration tank Secondary clarifier Influent Effluent Air supply Return sludge Excessive sludge
Activated sludge process Excessive sludge Effluent Secondary clarifier Influent Return sludge Aeration tank Air supply

Traditionally, activated sludge process is used to remove organic carbon(COD) from wastewaters(municipal and Industries In the process, microorganism in the sludge obtain their energy for cell synthesis (growth)through breaking down organic compounds into inorganic compounds( carbon dioxide) with oxygen as an electron acceptor Since 1970s, eutrophication in inland waters results in the world-wide concern about nutrient(N, P)removal from wastewaters. Traditional activated sludge processes are expanded to be applied in successfully removing n and p from water and wastewaters
Traditionally, activated sludge process is used to remove organic carbon (COD) from wastewaters (municipal and industries). In the process, microorganism in the sludge obtain their energy for cell synthesis (growth) through breaking down organic compounds into inorganic compounds ( carbon dioxide) with oxygen as an electron acceptor. Since 1970s, eutrophication in inland waters results in the world-wide concern about nutrient (N, P) removal from wastewaters. Traditional activated sludge processes are expanded to be applied in successfully removing N and P from water and wastewaters

Nitrogen Removal (Nitrification and Denitrification) Nitrification NH++3/20 Nitrisomenas No-+H0+2H+ NO,+1/20 Nitrobacter NO Denitrification NO3+ Org Denitrifiers +co+ho+oh Nitrification and denitrification can be achieved in activated sludge process and biofilm process. However, activated sludge process is the most widely used process in municipal and industrial wastewater treatment
Nitrogen Removal (Nitrification and Denitrification) Nitrification NH 4 + + 3/2O 2 NO 2 - + H 2O + 2H + NO 2 - + 1/2O 2 NO 3 - Denitrification NO 3 - + Org N 2 + CO 2 + H 2O + OHNitrisomenas Nitrobacter Denitrifiers Nitrification and denitrification can be achieved in activated sludge process and biofilm process. However, activated sludge process is the most widely used process in municipal and industrial wastewater treatment

Single-stage Activated sludge Nitrogen Removal Process Mixed liquor return Effluent Influent Anoxic Aerobic Sludge return Excessive sludge
Single-stage Activated Sludge Nitrogen Removal Process Anoxic Aerobic Mixed liquor return Sludge return Excessive sludge Influent Effluent

Phosphorous Removal (BPR) Activated sludge processes with alternating anaerobic and aerobic conditions have been successfully used for enhanced biological phosphorous removal (EBPr) from wastewater. This anaerobic-aerobic alternation can be achieved either by spatial configuration of anaerobic and aerobic zones in series in continuous flow systems with sludge recycle or by temporal arrangement of anaerobic and aerobic periods in sequence batch reactors
Phosphorous Removal (EBPR ) Activated sludge processes with alternating anaerobic and aerobic conditions have been successfully used for enhanced biological phosphorous removal (EBPR) from wastewater. This anaerobic-aerobic alternation can be achieved either by spatial configuration of anaerobic and aerobic zones in series in continuous flow systems with sludge recycle or by temporal arrangement of anaerobic and aerobic periods in sequence batch reactors

Spatial Configuration of Anaerobic and Aerobic zones in Series in Continuous Flow Systems Anaerobic Aerobic Clarifier Inflow Outflow Sludge recycle Wasted sludge SBCOD PHA PO4-P Spatial configuration
Spatial Configuration of Anaerobic and Aerobic Zones in Series in Continuous Flow Systems Anaerobic Aerobic Clarifier Sludge recycle Inflow Wasted sludge Outflow SBCOD PHA Concentrations PO4-P Spatial configuration

Temporal Arrangement of Anaerobic and Aerobic in Sequence Batch Reactor Influent Fill Effluent Draw Anaerobic
Temporal Arrangement of Anaerobic and Aerobic in Sequence Batch Reactor Aerobic Anaerobic Settle Draw Fill Influent Effluent

Polyphosphate-accumulating bacteria(PAB) play an essential role for EBPr in the anaerobic-aerobic process To achieve high and stable phosphorous removal it is essential to maintain a high percentage of paB in the sludge of eBPR system
Polyphosphate-accumulating bacteria (PAB) play an essential role for EBPR in the anaerobic-aerobic process. To achieve high and stable phosphorous removal, it is essential to maintain a high percentage of PAB in the sludge of EBPR system

e The mechanism of proliferation of PAB can be described as follows It is ty pically observed in the anaerobic stage that the activated sludge releases P to the bulk solution with concomitant uptake of organic substrates In the subsequent aerobic stage, it takes up more P than has been released in the previous anaerobic stage. The P removed from the wastewater is accumulated in the cell as poly P. Poly phosphate is a high-energy compound and its hydrolysis can supply energy to various biochemical reactions in the cell. In the anaerobic stage, the hydrolysis of intracellular polyP enables PAB to obtain the energy they need to take up organic substrates Without electron acceptors (oxygen, No2 NO3), aerobic bacteria and denitrifying bacteria are unable to obtain the energy required for the utilization of organic substrates, and they are thus unable to compete with PAB. Therefore, the introduction of the anaerobic stage leads to the precedence of PAb and to a rise in phosphorus content of the sludge By withdrawing the phosphorus-rich sludge from the system as excess sludge, high phosphate removal efficiency can be achieved
The mechanism of proliferation of PAB can be described as follows. It is typically observed in the anaerobic stage that the activated sludge releases Pi to the bulk solution with concomitant uptake of organic substrates. In the subsequent aerobic stage, it takes up more Pi than has been released in the previous anaerobic stage. The Pi removed from the wastewater is accumulated in the cell as polyP. Polyphosphate is a high-energy compound and its hydrolysis can supply energy to various biochemical reactions in the cell. In the anaerobic stage, the hydrolysis of intracellular polyP enables PAB to obtain the energy they need to take up organic substrates. Without electron acceptors (oxygen, NO 2 -/NO 3 -), aerobic bacteria and denitrifying bacteria are unable to obtain the energy required for the utilization of organic substrates, and they are thus unable to compete with PAB. Therefore, the introduction of the anaerobic stage leads to the precedence of PAB and to a rise in phosphorus content of the sludge. By withdrawing the phosphorus-rich sludge from the system as excess sludge, high phosphate removal efficiency can be achieved
按次数下载不扣除下载券;
注册用户24小时内重复下载只扣除一次;
顺序:VIP每日次数-->可用次数-->下载券;
- 西安建筑科技大学:《水资源利用与保护》教学课件_19 水资源管理的信息化.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_18 水价管理.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_17 水资源管理概述.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_16 农业节水.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_15 水环境质量与水资源保护技术.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_14 水体污染概述.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_13 排放口工程.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_12 蓄水工程.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_11 取水工程.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_10 水资源开发利用综合规划.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_9 城市水量平衡.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_8 区域水量平衡.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_7 需水量和水资源可利用量.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_6 城市污水的水质特点及可处理性双语课件.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_5 地下水资源.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_4 地表水资源.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_3 水循环和水资源概论双语课件.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_2 水循环和水资源.pdf
- 西安建筑科技大学:《水资源利用与保护》教学课件_1 绪论.pdf
- 西安建筑科技大学:《水资源利用与保护》课程研讨_西安市水环境变迁.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Case GM Ramon Arizpe Mexico.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Case GM Ramos Arizpe Mexicol.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_EPA - REMOVAL OF ARSENIC IN DRINKING WATER.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_General Introduction of Sewer System.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Review of Arsenic in natural water - Smedly.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_The arsenic problem - removal of arsenic.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Wastewater as a resource - EuroCase Paris.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Norge water and water technologies.pps
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Wastewater as a resource.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Wastewater characteristics.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Water reuse and recycling.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_Water Reuse.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_北京市区污水再生利用总体构想.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_城市污水再生回用的经济学思考.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_高等学校污水再生利用的途径与效益研究.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_缓解开封市水资源短缺的技术及工程措施研究.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_秦港污水再生回用工程的设计特色及综合效益分析.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_连续特枯年份下呼包平原水资源短缺的对策研究.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_中水回用是解决锦州市地下水资源短缺行之有效的重要途径.pdf
- 西安建筑科技大学:《水资源利用与保护》参考资料_Wastewater as a resource_全球气候变化使我国部分流域出现水资源短缺.pdf