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浸没式膜生物反应器处理酿酒厂废水

Treatment of winery wastewaters in a membrane submerged bioreactor.

作者信息

Artiga P, Carballa M, Garrido J M, Méndez R

机构信息

Deptartment of Chemical Engineering, School of Engineering, University of Santiago de Compostela, Rúa Lope Gómez de Marzoa, s/n, E-15782 Santiago de Compostela, Spain.

出版信息

Water Sci Technol. 2007;56(2):63-9. doi: 10.2166/wst.2007.473.

DOI:10.2166/wst.2007.473
PMID:17849979
Abstract

Wine production is seasonal, and thus the wastewater flow and its chemical oxygen demand (COD) concentrations greatly vary during the vintage and non-vintage periods, as well as being dependant on the winemaking technologies used, e.g. red, white or special wines production. Due to this seasonal high variability in terms of organic matter load, the use of membrane biological reactors (MBR) could be suitable for the treatment of such wastewaters. MBR offers several benefits, such as rapid start up, good effluent quality, low footprint area, absence of voluminous secondary settler and its operation is not affected by the settling properties of the sludge. A pilot scale hollow fibre MBR system of 220 L was fed by adequately diluting white wine with tap water, simulating wastewaters generated in wineries. The COD in the influent ranged between 1,000 and 4,000 mg/L. In less than 10 days after the start up, the system showed a good COD removal efficiency. The COD elimination percentage was always higher than 97% regardless of the organic loading rate (OLR) applied (0.5-2.2 kg COD/m3 d), with COD concentrations in the effluent ranging between 20 and 100 mg/L. Although the biomass concentration in the reactor increased from 0.5 to 8.6 g VSS/L, the suspended solids concentration in the effluent was negligible. Apparent biomass yield was estimated in 0.14 g VSS/g COD.

摘要

葡萄酒生产具有季节性,因此在收获季节和非收获季节,废水流量及其化学需氧量(COD)浓度会有很大变化,并且还取决于所使用的酿酒技术,例如红葡萄酒、白葡萄酒或特种葡萄酒的生产。由于有机物质负荷在季节上变化很大,使用膜生物反应器(MBR)可能适合处理此类废水。MBR具有诸多优点,例如启动迅速、出水水质良好、占地面积小、无需庞大的二次沉淀池,并且其运行不受污泥沉降性能的影响。一个220升的中试规模中空纤维MBR系统,通过用自来水充分稀释白葡萄酒来进水,模拟酒厂产生的废水。进水的COD范围在1000至4000毫克/升之间。在启动后不到10天,该系统就显示出良好的COD去除效率。无论应用的有机负荷率(OLR)如何(0.5 - 2.2千克COD/立方米·天),COD去除率始终高于97%,出水的COD浓度在20至100毫克/升之间。尽管反应器中的生物量浓度从0.5克挥发性悬浮固体/升增加到8.6克挥发性悬浮固体/升,但出水中的悬浮固体浓度可忽略不计。表观生物量产率估计为0.14克挥发性悬浮固体/克COD。

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