ZENGChao,LIUYing,CHENYuan,et al.Process Design and Efficiency Analysis of Nitrogen and Phosphorus Removal in Two Phases of a Reclaimed Water Plant[J].China Water & Wastewater,2024,40(18):64-70.
某再生水厂两期脱氮除磷工艺设计及效能分析
- Title:
- Process Design and Efficiency Analysis of Nitrogen and Phosphorus Removal in Two Phases of a Reclaimed Water Plant
- Keywords:
- reclaimed water plant; nitrogen and phosphorus removal; MSBR process; denitrification biological filter; high-efficiency air flotation; V?type filter; carbon emission
- 摘要:
- 某再生水厂一期采用“7池型MSBR+反硝化生物滤池+高效气浮”工艺,二期采用“10池型MSBR+深度脱氮V型滤池”工艺,设计出水水质均要求达到地表水准Ⅳ类标准(TN≤10 mg/L)。根据2022年1月—2023年7月的运营数据,一期平均出水TN为6.50 mg/L,TP为0.16 mg/L,平均吨水电耗为0.236 kW·h/m3,浓度为10%的液体PAC用量为28.97 mg/L,浓度为20%的液体碳源乙酸钠用量为63.17 mg/L,运行时的平均单位污染物碳排放强度为(4.59±0.98) kgCO2-eq/kg,吨水碳排放为(0.319±0.075) kgCO2-eq/m3;二期平均出水TN为5.37 mg/L,TP为0.19 mg/L,平均吨水电耗为0.273 kW·h/m3,浓度为10%的液体PAC用量为42.99 mg/L,浓度为20%的液体碳源乙酸钠用量为21.98 mg/L,运行时的平均单位污染物碳排放强度为(4.75±0.67) kgCO2-eq/kg,吨水碳排放为(0.328±0.050) kgCO2-eq/m3。
- Abstract:
- A reclaimed water plant adopts the process of 7-tank MSBR, denitrification biological filter and high-efficiency air flotation in phase I, and the process of 10-tank MSBR, deep denitrification V-type filter in phase Ⅱ. The design effluent quality is required to meet level quasi-Ⅳ criteria of Environmental Quality Standard for Surface Water (GB 3838-2002) , i.e., TN≤10 mg/L. According to relevant operation data from January 2022 to July 2023 in phase Ⅰ, the average effluent TN and TP were 6.50 mg/L and 0.16 mg/L, respectively. The corresponding average unit power consumption was 0.236 kW·h/m3, the dosage of 10% content liquid PAC was 28.97 mg/L, and the dosage of 20% content liquid carbon source sodium acetate was 63.17 mg/L. The average carbon emission intensity per unit pollutant during operation was (4.59±0.98) kgCO2-eq/kg,and the average carbon emission in tensity per ton of wastewater was (0.319±0.075) kgCO2-eq/m3. In phase Ⅱ, the average effluent TN was 5.37 mg/L, TP was 0.19 mg/L, the average unit power consumption was 0.273 kW·h/m3, the dosage of 10% content liquid PAC was 42.99 mg/L, and the dosage of 20% content liquid carbon source sodium acetate was 21.98 mg/L.The average unit carbon emission intensity was (4.75±0.67) kgCO2-eq/kg,and the average carbon emission in tensity per ton of wastewater was (0.328±0.050) kgCO2-eq/m3.
相似文献/References:
[1]王赛,时玉龙,蒋奇海,等.两种碳基材料对二级出水中有机物的去除特性[J].中国给水排水,2021,37(5):43.
WANG Sai,SHI Yu-long,JIANG Qi-hai,et al.Removal Characteristics of Organic Matters from Secondary Effluent by Two Types of Carbon Based Adsorbent[J].China Water & Wastewater,2021,37(18):43.
[2]何楠,王睿,彭柱,等.再生水厂混凝沉淀—微滤协同运行优化研究[J].中国给水排水,2021,37(7):85.
HE Nan,WANG Rui,PENG Zhu,et al.Optimization of Collaborative Operation of Coagulation-Sedimentation and Microfiltration in Reclaimed Water Treatment Plant[J].China Water & Wastewater,2021,37(18):85.
[3]黄良波,黄世浏,曹贵华,等.ABR-AO生化沉淀一体化污水处理工艺设计[J].中国给水排水,2022,38(2):54.
HUANG Liang-bo,HUANG Shi-liu,CAO Gui-hua,et al.Design of ABR-AO Biochemical Sedimentation Integrative Wastewater Treatment Process[J].China Water & Wastewater,2022,38(18):54.
[4]郑晓英,徐智,张远,等.纳米氧化铈对好氧污泥颗粒化进程的影响[J].中国给水排水,2022,38(3):21.
ZHENGXiao-ying,XUZhi,ZHANGYuan,et al.Effect of Cerium Oxide Nanoparticles on Aerobic Granulation Process[J].China Water & Wastewater,2022,38(18):21.
[5]王宏伟,张国珍,武福平,等.两级A/O生物滤池与微絮凝过滤组合处理二级出水[J].中国给水排水,2022,38(5):65.
WANGHong-wei,ZHANGGuo-zhen,WU Fu-ping,et al.Two?stage A/O Biofilter Combined with Micro-flocculation Filtration for Secondary Effluent Treatment[J].China Water & Wastewater,2022,38(18):65.
[6]崔涛,李胜,田敏,等.氧化沟型A2/O工艺脱氮除磷性能评价[J].中国给水排水,2022,38(7):75.
CUITao,LISheng,TIANMin,et al.Evaluation of Nitrogen and Phosphorus Removal Performance in an Oxidation Ditch Based A2/O Process[J].China Water & Wastewater,2022,38(18):75.
[7]曾晓岚,尹嘉豪,陈亮,等.电化学工艺处理滇池流域农业面源污水[J].中国给水排水,2022,38(13):105.
ZENGXiao-lan,YINJia-hao,CHENLiang,et al.Electrochemical Process for Treatment of Agricultural Non-point Source Sewage in Dianchi Basin[J].China Water & Wastewater,2022,38(18):105.
[8]何春求,周少奇.改良A2/O—MBR工艺仿真模拟及运行优化[J].中国给水排水,2022,38(15):90.
HEChun-qiu,ZHOUShao-qi.Simulation of Modified A2/O-MBR Process and Its Operation Optimization[J].China Water & Wastewater,2022,38(18):90.
[9]刘流,倪黄蕾,梁军,等.二沉池不同径向分布活性污泥对脱氮除磷的影响[J].中国给水排水,2022,38(15):104.
LIULiu,NIHuang-lei,LIANGJun,et al.Effect of Different Radial Distribution of Activated Sludge on Nitrogen and Phosphorus Removal in Secondary Settling Tank[J].China Water & Wastewater,2022,38(18):104.
[10]李易寰,董玉明,高芳.AAOA-MBR工艺在污水厂提标扩建中的应用[J].中国给水排水,2022,38(18):114.
LIYi-huan,DONGYu-ming,GAOFang.Application of AAOA-MBR Process in Sewage Treatment Plant Upgrading and Expansion[J].China Water & Wastewater,2022,38(18):114.