Xin Xin, Li BaiXue, Liu Xin, Yang Wenyu, Liu Qin
School of Resources and Environment, Chengdu University of Information Technology,Chengdu, 610225, China.
School of Resources and Environment, Chengdu University of Information Technology,Chengdu, 610225, China.
J Environ Manage. 2023 Apr 1;331:117298. doi: 10.1016/j.jenvman.2023.117298. Epub 2023 Jan 18.
A novel coupling process (SAPD-A) with sulfide autotrophic partial denitrification (SAPD) (NO-N→NO-N) and anaerobic ammonium oxidation (Anammox) was developed using anaerobic sequencing batch reactor (ASBR) in this work. The integrated process comprised two stages. Firstly, the starting-up of SAPD process succeeded by gradually increasing the influent nitrate and sulfide in 95 days. The average nitrate removal efficiency (NRE) and NO-N accumulation rates were 71.24% ± 0.21% and 46.44% ± 0.53% at SAPD process (days 75-95). Then, successful coupling process (SAPD-A) was implemented in two stages (stage I and stage II of SAPD-A). In stage I, it is feasible to promote the successful construction of SAPD-A process by elevating influent ammonium only based on SAPD system, making the NRE increased from 44.45% ± 0.46% (day 95) to 64.62% ± 0.12% at the end of stage I in SAPD-A system (day 126). Meanwhile, the ammonium nitrogen removal efficiency (ARE) and total nitrogen removal efficiency (TN-RE) also rose up to 42.46% ± 2.02% and 63.28% ± 0.54% respectively. Furthermore, the average ARE, NRE and TN-RE during the stage II in the bioreactor could reach 65.17% ± 1.45%, 74.50% ± 0.81% and 77.81% ± 0.37% by loading some biofilters (with of approximate 10% of the volume of the bioreactor) attached anaerobic ammonium oxidation bacteria (AnAOB). High-throughput sequencing results showed that the dominant genera concerning nitrogen removal were norank_f_norank_o_Fimbriimonadates (with the abundance of 2.88-8.54%), norank_ o_ norank _ c_ OM190 (2.48-4.41%), norank_f_norank_o_norank_c_WWE3 (11.01-17.69%), subgroup_10 (1.97-3.81%), Limnobacter(2.17-3.49%), norank_f_n orank_ o_norank_ c_OLB14 (2.03-5.23%), norank-f-PHOS-HE36 (2.18-5.5%), Ellin6067 (1.34-2.24%) and Candidatus_ Brocadia (1.95-2.42%) during the whole starting-up period of coupling SAPD-A process. Batch experiments revealed that the sulfide was fully oxidized within 2 h, with the maximum reaction rate of 38.30 ± 1.53 mg (L h) in the first 1 h. Simultaneously, the concentration of nitrate sharply decreased from 53.08 ± 0.23 mg L to 24.16 ± 0.42 mg L with the reaction rate of 66.41 ± 2.12 mg (L h) in 0.5 h. Also, the ammonium concentration significantly declined from 47.88 ± 0.34 mg L to 10.98 ± 0.39 mg L in 8 h. Anammox process was responsible for the dominant nitrogen removal in the coupling SAPD-A system.
本研究采用厌氧序批式反应器(ASBR)开发了一种新型耦合工艺(SAPD-A),该工艺将硫化物自养部分反硝化(SAPD,NO-N→NO-N)与厌氧氨氧化(Anammox)相结合。该集成工艺包括两个阶段。首先,通过在95天内逐渐增加进水硝酸盐和硫化物,成功启动了SAPD工艺。在SAPD工艺阶段(第75 - 95天),平均硝酸盐去除效率(NRE)和NO-N积累率分别为71.24% ± 0.21%和46.44% ± 0.53%。然后,在两个阶段(SAPD-A的阶段I和阶段II)实施了成功的耦合工艺(SAPD-A)。在阶段I,仅基于SAPD系统通过提高进水铵来促进SAPD-A工艺的成功构建是可行的,使得在SAPD-A系统阶段I结束时(第126天),NRE从44.45% ± 0.46%(第95天)提高到64.62% ± 0.12%。同时,铵氮去除效率(ARE)和总氮去除效率(TN-RE)也分别提高到42.46% ± 2.02%和63.28% ± 0.54%。此外,通过加载一些附着厌氧氨氧化细菌(AnAOB)的生物滤池(体积约为生物反应器体积的10%),生物反应器在阶段II期间的平均ARE、NRE和TN-RE可分别达到65.17% ± 1.45%、74.50% ± 0.81%和77.81% ± 0.37%。高通量测序结果表明,在耦合SAPD-A工艺的整个启动期间,参与氮去除的优势菌属为norank_f_norank_o_Fimbriimonadates(丰度为2.88 - 8.54%)、norank_ o_ norank _ c_ OM190(2.48 - 4.41%)、norank_f_norank_o_norank_c_WWE3(11.01 - 17.69%)、subgroup_10(1.97 - 3.81%)、Limnobacter(2.17 - 3.49%)、norank_f_n orank_ o_norank_ c_OLB14(2.03 - 5.23%)、norank-f-PHOS-HE36(2.18 - 5.5%)、Ellin6067(1.34 - 2.24%)和Candidatus_ Brocadia(1.95 - 2.42%)。批次实验表明,硫化物在2小时内被完全氧化,前1小时的最大反应速率为38.30 ± 1.53 mg/(L·h)。同时,硝酸盐浓度在0.5小时内从53.08 ± 0.23 mg/L急剧降至24.16 ± 0.42 mg/L,反应速率为66.41 ± 2.12 mg/(L·h)。此外,铵浓度在8小时内从47.88 ± 0.34 mg/L显著降至10.98 ± 0.39 mg/L。厌氧氨氧化工艺是耦合SAPD-A系统中主要的氮去除途径。