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通过亚硝酸盐进行生物去除的比较与好氧颗粒污泥和絮状活性污泥的实时控制。

Comparison of biological removal via nitrite with real-time control using aerobic granular sludge and flocculent activated sludge.

机构信息

School of Forestry, Northeast Forestry University, 26 Hexing Road, Harbin 150040, Heilongjiang Province, People's Republic of China.

出版信息

Appl Microbiol Biotechnol. 2011 Mar;89(5):1645-52. doi: 10.1007/s00253-010-2950-3. Epub 2010 Oct 23.

Abstract

The process of nitrification-denitrification via nitrite for nitrogen removal under real-time control mode was tested in two laboratory-scale sequencing batch reactors (SBRs) with flocculent activated sludge (R1) and aerobic granular sludge (R2) to compare operational performance and real-time control strategies. The results showed that the average ammonia nitrogen, total inorganic nitrogen (TIN), and chemical oxygen demand (COD) removal during aeration phase were 97.6%, 57.0%, and 90.1% in R2 compared with 98.6%, 48.7%, and 88.1% in R1. The TIN removed in both SBRs was partially due to the presence of simultaneous nitrification-denitrification via nitrite, especially in R2. The specific nitrification and denitrification rates in R2 were 0.0416 mg NH₄+ -N/gSS-min and 0.1889 mg NO X)⁻-N/gSS-min, which were 1.48 times and 1.35 times that of R1. The higher rates for COD removal, nitrification, and denitrification were achieved in R2 than R1 with similar influent quality. Dissolved oxygen (DO), pH, and oxidization reduction potential, corresponding to nutrient variations, were used as diagnostic parameters to control the organic carbon degradation and nitrification-denitrification via nitrite processes in both SBRs. The online control strategy of granular SBR was similar to that of the SBR with flocculent activated sludge. However, a unique U-type pattern on the DO curve in granular SBR was different from SBR with flocculent activated sludge in aerobic phase.

摘要

在实时控制模式下,通过亚硝酸盐进行硝化-反硝化脱氮的过程在两个具有絮状活性污泥(R1)和好氧颗粒污泥(R2)的实验室规模序批式反应器(SBR)中进行了测试,以比较运行性能和实时控制策略。结果表明,与 R1 相比,在 R2 中曝气阶段的平均氨氮、总无机氮(TIN)和化学需氧量(COD)去除率分别为 97.6%、57.0%和 90.1%,而 R1 中的去除率分别为 98.6%、48.7%和 88.1%。两个 SBR 中去除的 TIN 部分是由于同时存在通过亚硝酸盐进行的硝化-反硝化,尤其是在 R2 中。R2 的特定硝化和反硝化速率分别为 0.0416mgNH₄+-N/gSS-min 和 0.1889mgNO X- -N/gSS-min,分别是 R1 的 1.48 倍和 1.35 倍。在类似进水质量的情况下,R2 实现了比 R1 更高的 COD 去除率、硝化率和反硝化率。溶解氧(DO)、pH 值和氧化还原电位,对应于营养物质的变化,被用作控制有机碳降解和两个 SBR 中通过亚硝酸盐进行的硝化-反硝化过程的诊断参数。颗粒 SBR 的在线控制策略与絮状活性污泥 SBR 相似。然而,在颗粒 SBR 中 DO 曲线的独特 U 型模式与好氧阶段的絮状活性污泥 SBR 不同。

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