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AnSBBR 应用于个人护理行业废水处理:填充时间、每个周期处理的体积和有机负荷的影响。

AnSBBR applied to a personal care industry wastewater treatment: effects of fill time, volume treated per cycle, and organic load.

机构信息

Escola de Engenharia Mauá (EEM), Instituto Mauá de Tecnologia (IMT), Praça Mauá 1, São Caetano do Sul, São Paulo, Brazil.

出版信息

Appl Biochem Biotechnol. 2011 Jan;163(1):127-42. doi: 10.1007/s12010-010-9022-0. Epub 2010 Dec 10.

DOI:10.1007/s12010-010-9022-0
PMID:21153450
Abstract

A study was performed regarding the effect of the relation between fill time, volume treated per cycle, and influent concentration at different applied organic loadings on the stability and efficiency of an anaerobic sequencing batch reactor containing immobilized biomass on polyurethane foam with recirculation of the liquid phase (AnSBBR) applied to the treatment of wastewater from a personal care industry. Total cycle length of the reactor was 8 h (480 min). Fill times were 10 min in the batch operation, 4 h in the fed-batch operation, and a 10-min batch followed by a 4-h fed batch in the mixed operation. Settling time was not necessary since the biomass was immobilized and decant time was 10 min. Volume of liquid medium in the reactor was 2.5 L, whereas volume treated per cycle ranged from 0.88 to 2.5 L in accordance with fill time. Influent concentration varied from 300 to 1,425 mg COD/L, resulting in an applied volumetric organic load of 0.9 and 1.5 g COD/L.d. Recirculation flow rate was 20 L/h, and the reactor was maintained at 30 °C. Values of organic matter removal efficiency of filtered effluent samples were below 71% in the batch operations and above 74% in the operations of fed batch followed by batch. Feeding wastewater during part of the operational cycle was beneficial to the system, as it resulted in indirect control over the conversion of substrate into intermediates that would negatively interfere with the biochemical reactions regarding the degradation of organic matter. As a result, the average substrate consumption increased, leading to higher organic removal efficiencies in the fed-batch operations.

摘要

进行了一项研究,旨在探讨在不同施加有机负荷下,填充时间、每个循环处理的体积和进水浓度之间的关系对含有固定化生物量的循环式厌氧序批式反应器(AnSBBR)的稳定性和效率的影响,该反应器应用于个人护理行业废水的处理。反应器的总循环时间为 8 小时(480 分钟)。在批处理操作中,填充时间为 10 分钟,在进料批处理操作中为 4 小时,在混合操作中,先进行 10 分钟的批处理,然后进行 4 小时的进料批处理。由于生物量被固定化,因此不需要沉淀时间,排泥时间为 10 分钟。反应器中的液体介质体积为 2.5 升,而每个循环处理的体积根据填充时间从 0.88 升至 2.5 升。进水浓度从 300 升至 1425mg COD/L,导致施加的体积有机负荷为 0.9 和 1.5g COD/L.d。循环流量为 20L/h,反应器保持在 30°C。在批处理操作中,过滤出水样品的有机物去除效率值低于 71%,而在进料批处理后进行批处理的操作中,该值高于 74%。在操作过程的部分阶段中,进料废水有利于系统,因为它可以间接控制基质转化为中间体,这会对有机物降解的生化反应产生负面影响。因此,平均基质消耗增加,导致进料批处理操作中的有机物去除效率更高。

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