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200t/h Domestic Sewage Treatment Process Design

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英文文摘

论文说明:ABBREVIATIONS AND SYMBOLS

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ACKNOWLEDGEMENTS

CHAPTER 1 INTRODUCTION AND WASTEWATER TREATMENT PROCESS DETERMINATION

1.0 INTRODUCTION

1.1 LITERATURE REVIEW

1.1.1 Wastewater treatment overview

1.1.2 Biological treatment overview

1.2 DOMESTIC SEWAGE TREATMENT PROCESS

1.2.1 Treatment process determination

1.2.2 Flow sheet determination

1.2.3 Design limits

1.3 FUNDAMENTALS OF SEWAGE TREATMENT

1.3.1 Biological nutrients removal processes

1.3.2 Development of controlled biological nutrient removal

1.3.3 Commonly applied BNR process configurations

1.3.4 Nitrogen Removal

1.3.5 Phosphorus Removal

1.3.6 Design standards

1.4 FLOW SHEET EXPLATIONS

1.4.1 Biological selector

1.4.2 Description of selected domestic wastewater facility

CHAPTER 2 DESIGN AND TECHNOLOGICAL CALCULATIONS

2.1 Operating and design parameters

2.1.1 Solids retention time for denitrification, SRTDN

2.1.2 Yield coefficient for denitrification

2.1.3 Design solids retention time for aerobic cell growth, SRTaerobic

2.1.4 Design cell yield caused by BOD5 removal

2.1.5 Design cell yield caused by nitrification (Yobs, N)

2.1.6 Design cell yield caused by cell debris production

2.1.7 Soluble BOD5 in the effluent

2.2 Preliminary and primary treatments

2.2.1 Design of bar rack (coarse screen)

2.2.2 Design of grit chamber

2.2.3 Equalization tank

2.2.4 Design of primary sedimentation tank

2.3 Material mass balance analysis

2.3.1 First iteration

2.3.2 Second iteration

2.4 pH control and alkalinity needed

2.5 Oxygen requirements

2.6 BNR system design: sizing and configuration

2.6.1 Anaerobic tank

2.6.2 Anoxic bioreactor

2.6.3 Aerobic bioreactor

2.6.4 CAAA reactor configuration

2.7 Solids separation facility design

2.7.1 Surface area of Secondary Clarifier

2.7.2 Depth of Secondary Clarifier

2.7.3 Detention time

2.8 Disinfection facility design

2.8.1 Disinfection effectiveness

2.8.2 Required chlorine dioxide dosage for disinfection

2.8.3 Contact Basin

2.8.4 Design contact basin based on dispersion

2.9 Plant layout

CHAPTER 3 EQUIPMENTS SELECTION AND MATERIAL CONSUMPTION

3.1 EQUIPMENTS TECHNOLOGICAL CALCULATIONS AND SELECTION

3.1.1 Bar rack (coarse screen)

3.1.2 Aerated grit chamber equipment

3.1.3 Equalization effluent pump

3.1.4 Primary sludge pump

3.1.5 Primary sedimentation tank equipment

3.1.6 Sludge collection system and skimmer

3.1.7 Primary effluent pump

3.1.8 Waste activated sludge system

3.1.9 Internal recycle pump

3.1.10 Secondary effluent pump

3.1.11 Return sludge pumps

3.1.12 Mixer power requirement for anaerobic and anoxic tanks ones

3.1.13 Design capacity of air supply system

3.1.14 Design capacity diffused aeration system and Blower sizing

3.2 EQUIPMENT LIST

3.3 MATERIAL CONSUMPTION AND QUANTITY

CHAPTER 4 COST ESTIMATION PROCESS SAFETY EVALUATION AND CONCLUSION

4.1 WORKSHOP AND COST ESTIMATION

4.1.1 Preliminary treatment (coarse screen with grit removal)

4.1.2 Primary sedimentation with sludge pump

4.1.3 Conventional activated sludge with diffused air

4.1.4 Final clarifier

4.1.5 Disinfection

4.1.6 Miscellaneous structures

4.1.7 Support personnel

4.2 ENVIRONMENTAL AND FIRE PROTECTION, PROCESS SAFETY AND HEALTH

4.2.1 Failure-Mode Effect Analysis

4.2.2 Process hazard and operability (HAZOP)

4.3 CONCLUSION AND DISCUSSION

DISCUSSION

REFERENCES

APPENDICES

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摘要

论文系统地给出了采用物理法和生物法相结合进行生活污水处理过程的工艺设计。为实现目标,在污水处理工艺设计过程中对过程单元、层次结构进行了全流程分析,提出了一种把化学、物理、生物方法集成在同一系统的低成本处理生活污水的途径。 过程的工艺设计内容分五个部分: (1)生活污水处理流程的确定; (2)处理过程基本原理; (3)工艺设计计算和设备选型; (4)项目费用估算; (5)装置系统的环保、防火、安全卫生等评价。 生活污水主要经过预处理(除砂),初级处理,生物脱氮除磷系统及消毒等单元的操作。当工艺条件为:[温度25℃;预处理设备(格栅池及曝气沉砂池,停留时间5分钟);初级沉降池(停留时间1.8小时);生物脱氮除磷系统(二级处理过程):厌氧反应器(水力停留时间1.5小时),无氧反应器(水力停留时间1.5小时,系统反应时间5天),需氧反应器(水力停留时间3小时,系统反应时间5天)]时,过程有很高的去除率:其中:BOD5和TSS去除率为95%,N和P的去除率约为为80%。经本装置处理后的排出水质符合中华人民共和国生活污水排放一级标准。

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