摘要
从内碳源有效利用角度出发,开发了新型连续流后置反硝化AOA工艺,将厌氧段混合液按一定比例分流至缺氧段,从而强化缺氧段反硝化除磷作用.进水NH+4-N和PO3-4-P浓度保持在(38.31±2.03)mg·L-1和(5.74±0.13)mg·L-1,在不同运行阶段进水COD分别控制在300mg·L-1和250 mg·L-1,考察了AOA工艺处理低C/N(C/P)比污水过程影响因素.当进水C/N比和C/P比分别为7.41±0.26和52.36±1.25时,通过将SRT由10 d延长到16 d,系统TN和PO3-4-P去除率分别稳定在65.86%±2.06%和90.00%±3.97%;当进水C/N比、C/P比降至6.14±0.32和43.40±1.37时,在SRT为16 d条件下,将A/O/A体积比由1/3/1调整为1/2/2,TN和PO3-4-P去除率分别升至69.76%±3.36%和98.73%±1.82%.结果表明,采用控制SRT、调整好氧/缺氧HRT等策略,可保证处理低C/N(C/P)比污水AOA工艺高效稳定运行.
Based on the efficient utilization of internal carbon source, a novel post-anoxic continuous anaerobic/aerobic/anoxic (AOA) process was developed. In this process, part of the anaerobic mixed liquor was transferred to the post-anoxic zone in order to enhance the denitrifying phosphorous removal. The influent NH4+-N and PO43--P concentrations were maintained at (38.312.03) mgL-1 and (5.740.13) mgL-1, and the influent COD concentration was controlled at 300 mgL-1 and 250 mgL-1 during different operating periods. The effect of operating parameters on nutrient removal performance of the AOA process in treating the wastewater with low C/N and C/P ratios was also investigated. It was found that with influent C/N and C/P ratios of 7.410.26 and 52.361.25, respectively, the removal efficiencies of TN and PO43--P reached 65.86%2.06% and 90.00%3.97% along with the SRT from 10 d to 16 d. When influent C/N and C/P ratios decreased to 6.140.32 and 43.401.37, the removal efficiencies of TN and PO43--P increased to 69.76%3.36% and 98.73%1.82% via the change of A/O/A ratio from 1/3/1 to 1/2/2. It was therefore concluded that the nutrient removal performance of the AOA process in treating wastewater with low C/N and C/P ratios could be stable by controlling SRT as well as aerobic and anoxic HRTs.
出处
《环境科学学报》
CAS
CSCD
北大核心
2013年第11期2979-2986,共8页
Acta Scientiae Circumstantiae
基金
粤港关键领域重点突破项目(No.2009A030902002)
国家水体污染控制与治理重大科技专项(No.2012ZX07206-002)~~
关键词
生物脱氮除磷
后置反硝化
反硝化除磷
内碳源
C
N比
C
P比
biological nutrient removal
post-anoxic process
denitrifying phosphorous removal
internal carbon source
C/N ratio
C/P ratio