START-UP OF SBR-PN PROCESS AND N2O EMISSION IN SIDE PRETREATMENT OF WASTED SLUDGE BY FREE NITROUS ACID
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摘要: 在序批式生物反应器(SBR)基础上增设游离亚硝酸(FNA)污泥预处理单元,成功启动了SBR短程硝化(SBR-PN)过程。FNA对NOB的活性抑制远大于其对AOB的抑制,FNA=0.48 mg/L,两者活性差异最大。SBR运行稳定(阶段Ⅰ)后,利用0.48 mg/L的FNA对活性污泥进行24 h缺氧处理,经60 d驯化(阶段Ⅱ),SBR内NH4+-N去除率和亚硝态氮积累率(NAR)均达到95%以上,总氮(TN)去除率由(22.8±3.6)%增至(35.5±3.7)%。分段进水(阶段Ⅲ)方式提高了原水有机物利用率,TN去除率达到(64.0±2.5)%,最大NO2-积累和N2O产量分别由(16.4±1.6) mg/L和(0.85±0.09) mg/L降至(11.4±1.2) mg/L和(0.28±0.04) mg/L,N2O产率由(7.40±0.99)%降至(1.33±0.26)%。基于FNA缺氧抑菌选择性差异,采用分段进水方式运行SBR,防止了高浓度NO2-和NH4+共存,可实现稳定生活污水短程硝化过程并降低N2O释放。经FNA处理,活性污泥蛋白质(PN)和多糖(PS)释放增加,PN/PS由阶段Ⅰ的1.42增至阶段Ⅱ、Ⅲ的1.77和1.74,SVI由阶段Ⅰ的(113±12) mL/gVSS分别增至阶段Ⅱ、Ⅲ的(129±15),(122±13) mL/gVSS。Abstract: The start up of partial nitrification by using free nitrous acid(FNA) to treat activated sludge was studied in a sequencing batch reactor(SBR) treating rural wastewater by recirculating a portion of the sludge through a side-stream sludge treatment unit. FNA is substantially more biocidal to NOB than to AOB. The difference was the highest at the FNA concentration of 0.48 mg/L. With 3.6 L activated sludge treated by 0.48 mg/L FNA for 24 h under anoxic condition each day, the stable partial nitrification in the sequencing batch reactor(SBR-PN) was established after 60 d accumulation, with the NH4+ removal efficiency and the nitrite accumulation rate(NAR) were both above 95%(Stage Ⅱ). The two-step feeding strategy(Stage Ⅲ) was used to replace the one-step feeding in the SBR with the aim to reduce the NO2- accumulation and N2O emission. The results showed that the maximum NO2- accumulation and N2O emission were reduced from(16.4±1.6) mg/L and(0.85±0.09) mg/L to(11.4±1.2) mg/L and(0.28±0.04) mg/L, respectively, with the TN removal efficiency of(64.0±2.5)%, the N2O yield decreased from(7.40±0.99)% to(1.33±0.26)%. Based on the selectivity of FNA on AOB and NOB, the coexistence of high NO2- and NH4+ was prevented by two-step feeding strategy of the SBR, which was beneficial to the establishment of partial nitrification and the reduction of N2O emission. PN/PS value increased from 1.42 in stage Ⅰ to 1.77 and 1.74 in stage Ⅱ and Ⅲ, additionally, SVI increased from(113±12) mL/gVSS to(129±15) mL/gVSS in stage Ⅱ and(122±13) mL/gVSS in stage Ⅲ respectively.
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Key words:
- free nitrous acid /
- sludge treatment /
- partial nitrification /
- nitrous oxide /
- EPS
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