CHENShan-shan,WANGXiao-dong,ZHOUXiao-lin,et al.Determination of Active Biomass and Its Distribution in Enhanced Denitrification MBBR[J].China Water & Wastewater,2022,38(15):73-77.
强化脱氮MBBR中活性生物量的测定及其分布
- Title:
- Determination of Active Biomass and Its Distribution in Enhanced Denitrification MBBR
- 摘要:
- 设计开发了强化脱氮移动床生物膜反应器(MBBR)中试系统,采用耗氧呼吸速率法研究了各反应单元中的活性生物量分布情况,并分析了不同进水负荷对各单元中活性生物量的影响。研究发现,各反应单元生物膜中的异养活性生物量占比均在60%以上。缺氧单元每个填料上的异养活性生物量平均为0.56~0.86 mg/L(以COD计,下同),好氧单元的自养活性生物量占比可达到37.6%。此外,当SCOD负荷增加0.80~9.70 g/(m2·d)时,异养活性生物量可增加0.19~0.53 mg/L;当氨氮负荷增加0~1.15 g/(m2·d)时,自养活性生物量可增加0~0.11 mg/L。
- Abstract:
- A pilot?scale enhanced denitrification MBBR was developed. The distribution of the active biomass in each unit was investigated by oxygen uptake rate method, and the effects of different influent loads on the active biomass in each unit were analyzed. The proportion of heterotrophic active biomass in biofilm of each unit was more than 60%. The average heterotrophic active biomass of each filler in anoxic unit was between 0.56-0.86 mg/L, and the proportion of autotrophic active biomass in aerobic units accounted for 37.6%. When SCOD load increased by 0.80-9.70 g/(m2·d), heterotrophic active biomass increased by 0.19-0.53 mg/L. When ammonia nitrogen load increased by 0-1.15 g/(m2·d), autotrophic active biomass increased by 0-0.11 mg/L.
相似文献/References:
[1]朱点钰,陈年浩,朱津苇,等.填料类型对MBBR启动及运行效能的影响[J].中国给水排水,2018,34(21):1.
ZHU Dian yu,CHEN Nian hao,ZHU Jin wei,et al.Effect of Carrier Type on Startup and Operating Efficiency of Moving Bed Biofilm Reactor[J].China Water & Wastewater,2018,34(15):1.
[2]郑临奥,吴迪,张晶晶,等.城市污水泵站改为河道生态补给站的实践总结[J].中国给水排水,2018,34(20):82.
ZHENG Lin ao,WU Di,ZHANG Jing jing,et al.Practice of River Ecological Replenishment Retrofitting from an Urban Sewage Pumping Station[J].China Water & Wastewater,2018,34(15):82.
[3]郭莉芳,朱宇峰,滕良方,等.MBBR用于南方某污水厂强化脱氮效果分析[J].中国给水排水,2020,36(7):101.
[4]周家中,吴迪,郑临奥.纯膜MBBR工艺在国内外的工程应用[J].中国给水排水,2020,36(22):37.
ZHOU Jia-zhong,WU Di,ZHENG Lin-ao.Engineering Application of Pure MBBR Process at Home and Abroad[J].China Water & Wastewater,2020,36(15):37.
[5]杨平,周家中,管勇杰,等.基于MBBR的AAO和Bardenpho工艺改造效果对比[J].中国给水排水,2021,37(7):11.
YANG Ping,ZHOU Jia-zhong,GUAN Yong-jie,et al.Comparison of AAO and Bardenpho Processes Transformation Effect Based on MBBR[J].China Water & Wastewater,2021,37(15):11.
[6]孙庆花,张晓霞,赵益华,等.天津某高盐高排放标准污水厂提标改造工程设计[J].中国给水排水,2021,37(8):83.
SUN Qing-hua,ZHANG Xiao-xia,ZHAO Yi-hua,et al.Design of a Wastewater Treatment Plant Upgrading Project with High Salinity Influent and High Discharge Standard in Tianjin[J].China Water & Wastewater,2021,37(15):83.
[7]周家中,宋平周,张爽,等.占地受限下北方某高标准新建污水厂工程设计[J].中国给水排水,2021,37(12):76.
ZHOU Jia-zhong,SONG Ping-zhou,ZHANG Shuang,et al.Engineering Design of a New High-standard Wastewater Treatment Plant with Limited Footprint Area in North China[J].China Water & Wastewater,2021,37(15):76.
[8]陈如勇,张晓霞,周家中,等.MSBR改为三级A/O-MBBR连续流工艺的应用效果[J].中国给水排水,2021,37(14):108.
CHEN Ru-yong,ZHANG Xiao-xia,ZHOU Jia-zhong,et al.Practical Application Effect of Retrofitted MSBR into Three-stage A/O-MBBR Continuous Flow Process[J].China Water & Wastewater,2021,37(15):108.
[9]王雪欣,毕学军,麻弛张,等.两点进水三段A/O-MBBR生物脱氮中试研究[J].中国给水排水,2021,37(17):62.
WANG Xue-xin,BI Xue-jun,MA Chi-zhang,et al.Nitrogen Removal of Pilot-scale Three Stages A/O-MBBR with Two-step-feed[J].China Water & Wastewater,2021,37(15):62.
[10]周小琳,樊星,毕学军,等.两段式A/O-MBBR工艺生物脱氮中试与系统优化[J].中国给水排水,2021,37(19):72.
ZHOU Xiao-lin,FAN Xing,BI Xue-jun,et al.Pilot-scale Test and System Optimization of Two-stage A/O-MBBR Process for Biological Nitrogen Removal[J].China Water & Wastewater,2021,37(15):72.