Suppr超能文献

两段式颗粒污泥亚硝化/厌氧氨氧化工艺处理城市生活垃圾有机部分厌氧消化液。

Two-stage granular sludge partial nitritation/anammox process for the treatment of digestate from the anaerobic digestion of the organic fraction of municipal solid waste.

机构信息

Politecnico di Milano, Department of Civil and Environmental Engineering (DICA), P.zza L. da Vinci, 32, 20133 Milano, Italy.

Politecnico di Milano, Department of Civil and Environmental Engineering (DICA), P.zza L. da Vinci, 32, 20133 Milano, Italy.

出版信息

Waste Manag. 2019 Dec;100:36-44. doi: 10.1016/j.wasman.2019.08.044. Epub 2019 Sep 26.

Abstract

The increasing amount of source separated organic fraction of municipal solid wastes (OFMSW) treated by anaerobic digestion for energy recovery requires the implementation of cost-efficient processes for the treatment of the produced digestate, especially in terms of nitrogen removal. The autotrophic nitrogen removal process, based on the coupling of two biological processes, partial nitritation (PN) and anammox (A), appears as a suitable solution due to important savings in operational costs compared to conventional treatment processes. However, its application could be hampered by the high salinity and inhibitory potential of this kind of digestate. In this contribution, two lab-scale granular sludge reactors performing the PN and anammox processes, respectively, were used to treat (opportunely diluted) real OFMSW digestate originating from full-scale biogas plants with the aim of assessing their treatment feasibility in a two-stage PN/A configuration. The PN process was implemented in an air-lift granular sludge reactor and was able to treat a nitrogen loading rate of about 1 g N L d at 30 ± 0.5 °C; moreover, its effluent was suitable for the subsequent anammox treatment, with an appropriate effluent NO/NH ratio and marginal inhibiting effects. In the anammox granular sludge reactor, the anammox activity was affected by high salinity levels, nonetheless a stable reactor performance at a nitrogen removing rate of 0.83 ± 0.20 and 0.31 ± 0.04 g N L d at 35 ± 0.5 °C, were achieved when treating 50% and 30% diluted real wastewaters at a conductivity in the reactor of 9.1 and 11.2 mS cm, respectively.

摘要

越来越多的经厌氧消化处理以回收能源的城市固体废物(MSW)的有机分离源部分(OFMSW)需要实施具有成本效益的工艺来处理所产生的消化物,特别是在脱氮方面。基于两个生物过程,即部分硝化(PN)和厌氧氨氧化(Anammox)偶联的自养脱氮工艺,由于与传统处理工艺相比可节省大量运营成本,因此似乎是一种合适的解决方案。然而,由于这种消化物的高盐度和抑制潜力,其应用可能会受到阻碍。在本研究中,分别使用两个实验室规模的颗粒污泥反应器来处理(适当稀释的)来自大型沼气厂的实际 MSW 消化物,以评估它们在两段式 PN/A 配置中进行处理的可行性。PN 工艺在气升式颗粒污泥反应器中实施,能够在 30±0.5°C 下处理约 1 g N L d 的氮负荷;此外,其出水适用于后续的厌氧氨氧化处理,具有适当的出水 NO/NH 比和较小的抑制作用。在厌氧氨氧化颗粒污泥反应器中,高盐度水平会影响厌氧氨氧化活性,但在 35±0.5°C 下,当处理 50%和 30%稀释的实际废水时,在反应器电导率分别为 9.1 和 11.2 mS cm 时,仍可达到 0.83±0.20 和 0.31±0.04 g N L d 的稳定脱氮速率。

文献AI研究员

20分钟写一篇综述,助力文献阅读效率提升50倍。

立即体验

用中文搜PubMed

大模型驱动的PubMed中文搜索引擎

马上搜索

文档翻译

学术文献翻译模型,支持多种主流文档格式。

立即体验