Jiangxi University of Science and Technology, School of Resources & Environmental Engineering, Jiangxi province, Ganzhou city 341000, PR China.
Jiangxi University of Science and Technology, School of Resources & Environmental Engineering, Jiangxi province, Ganzhou city 341000, PR China.
Sci Total Environ. 2019 Nov 20;692:741-755. doi: 10.1016/j.scitotenv.2019.07.308. Epub 2019 Jul 21.
Conventional nitrification/denitrification process is gradually being replaced with partial-nitritation/anammox (PN/A) processes due to its installation and running cost. However, high ammonia-oxidizing bacteria (AOB) and anaerobic ammonia-oxidizing (anammox) bacteria activity as well as optimum out-selection of nitrite-oxidizing bacteria (NOB) are necessary to achieving efficient PN/A process. Consequently, to enhance PN process via nitrifying bacteria enrichment/out-selection within psychrophilic environment, a novel pH-DO (dissolved oxygen) control strategy was proposed and the response of PN, kinetics, AOB enrichment, and NOB out-selection efficiency was investigated during start-up and long-term operation. With DO of 0.7 mg/L and pH of 7.5-7.9, quick start-up of the PN process was established within 34d as NO-N accumulation ratio (NAR) reached 90.08 ± 1.4%. Again, when NLR was elevated to 0.8 kg/m·d (400mgNH-N/L), DO curtailed to 0.2 mg/L, pH maintained at 7.7 and free ammonium at 6.5 mg/L, NAR and NH-N removal rate could still reach 97.04 ± 2.4% and 97.84 ± 1.5%, respectively. After optimum control factors had been established, real nitrogen-rich-mine-wastewater was fed (DO, 0.2 mg/L, pH, 8.9, and free ammonia, 6.5 mg/L) and NAR and NH-N removal rate reached was 97.33 ± 0.5% and 97.76 ± 1.1%, respectively. Estimated kinetic parameters including maximum degradation rate (Vmax = 1.58/d), half-rate constant (Km = 33.8 mg/L), and inhibition constant (Ki = 201.6 mg/L) suggested that inhibition on NH-N oxidation was most feasible at higher concentration of NH-N. To elucidate biological mechanisms, 16S rRNA high-throughput revealed that AOB (Nitrosomonas) enrichment had increased from 0.08% to 49% whereas NOB (Nitrospira) abundance reduced from 1% to 0.034%, indicating pH-DO control efficiently enriched AOB and out-selected NOB. Conversely, when influent NH-N was curtailed to about 200 mg/L and free ammonia concentration maintained at 6.5 mg/L, the population of AOB was observably reduced by 6% within a period of 14 days, indicating control strategies including pH-DO control and substrate availability were the key factors which substantially influenced and promoted the activities and growth of AOBs in the present SBR.
传统的硝化/反硝化工艺由于其安装和运行成本逐渐被部分硝化/厌氧氨氧化(PN/A)工艺所取代。然而,要实现高效的 PN/A 工艺,需要高氨氧化细菌(AOB)和厌氧氨氧化(anammox)细菌的活性以及亚硝酸盐氧化细菌(NOB)的最佳选择。因此,为了通过在低温环境中硝化细菌的富集/选择来增强 PN 工艺,提出了一种新的 pH-DO(溶解氧)控制策略,并在启动和长期运行期间研究了 PN、动力学、AOB 富集和 NOB 选择效率的响应。在 DO 为 0.7mg/L 和 pH 为 7.5-7.9 的条件下,PN 工艺在 34d 内快速启动,NO-N 积累比(NAR)达到 90.08±1.4%。再次,当 NLR 提高到 0.8kg/m·d(400mgNH-N/L)时,将 DO 削减至 0.2mg/L,将 pH 维持在 7.7,将游离氨控制在 6.5mg/L,NAR 和 NH-N 的去除率仍可分别达到 97.04±2.4%和 97.84±1.5%。在确定最佳控制因素后,处理实际的富氮矿山废水(DO 为 0.2mg/L,pH 为 8.9,游离氨为 6.5mg/L),NAR 和 NH-N 的去除率分别达到 97.33±0.5%和 97.76±1.1%。估计的动力学参数包括最大降解速率(Vmax=1.58/d)、半速率常数(Km=33.8mg/L)和抑制常数(Ki=201.6mg/L)表明,在较高的 NH-N 浓度下,对 NH-N 氧化的抑制作用最为明显。为了阐明生物机制,16S rRNA 高通量分析显示,AOB(亚硝化单胞菌)的丰度从 0.08%增加到 49%,而 NOB(硝化螺旋菌)的丰度从 1%减少到 0.034%,表明 pH-DO 控制有效地富集了 AOB,并选择了 NOB。相反,当进水 NH-N 减少到约 200mg/L 并将游离氨浓度维持在 6.5mg/L 时,AOB 的数量在 14 天内明显减少了 6%,这表明 pH-DO 控制和基质可用性等控制策略是影响和促进本 SBR 中 AOB 活性和生长的关键因素。