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Integrated Membrane Process for the Treatment and Reuse of Residual Table Olive Fermentation Brine and Anaerobically Digested Sludge Centrate

机译:用于处理和再利用残留的表橄榄发酵盐水和厌氧消化污泥的集成膜方法

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摘要

Management of wastewater is a major challenge nowadays, due to increasing water demand, growing population and more stringent regulations on water quality. Wastewaters from food conservation are especially difficult to treat, since they have high salinity and high organic matter concentration. The aim of this work is the treatment of the effluent from a table olive fermentation process (FTOP) with the aim of reusing it once the organic matter is separated. The process proposed in this work consists of the following membrane-based technologies: Ultrafiltration (UF) (UP005, Microdyn Nadir), Forward Osmosis (FO) (Osmen2521, Hydration Technology Innovation) and Nanofiltration (NF) (NF245, Dow). The FO process was implemented to reduce the salinity entering the NF process, using the FTOP as draw solution and, at the same time, to concentrate the centrate produced in the sludge treatment of a municipal wastewater treatment plant with the aim of obtaining a stream enriched in nutrients. The UF step achieved the elimination of 50% of the chemical oxygen demand of the FTOP. The UF permeate was pumped to the FO system reducing the volume of the anaerobically digested sludge centrate (ADSC) by a factor of 3 in 6.5 h. Finally, the ultrafiltrated FTOP diluted by FO was subjected to NF. The transmembrane pressure needed in the NF stage was 40% lower than that required if the ultrafiltration permeate was directly nanofiltered. By means of the integrated process, the concentration of organic matter and phenolic compounds in the FTOP decreased by 97%. Therefore, the proposed process was able to obtain a treated brine that could be reused in other processes and simultaneously to concentrate a stream, such as the ADSC.
机译:污水管理是如今的一个主要挑战,由于需水需求增加,人口不断增长,水质规定更严格。食物保护的废水尤其难以治疗,因为它们具有高盐度和高有机物质浓度。这项工作的目的是从表橄榄发酵过程(FTOP)中处理流出物,其目的是在分离有机物质后重新使用。本作工作中提出的过程包括以下基于膜的技术:超滤(UF)(UP)(UP005,MicroDeryn Nadir),前渗透(Fo)(OSMEN2521,水合技术创新)和纳米滤灰(NF)(NF245,Dow)。实施FO工艺以减少进入NF工艺的盐度,使用FTOP作为绘制溶液,同时浓缩在市政废水处理厂的污泥处理中产生的中心,以获得丰富的流在营养素中。 UF步骤取消了FTOP的50%的化学需氧量。将UF渗透物泵送到FO系统,将厌氧物质消化的污泥(ADSC)的体积减少6.5小时的倍数3。最后,对由FO稀释的超滤FTOP进行NF。如果超滤渗透物直接纳米过滤,则NF阶段所需的跨膜压力降低40%。通过综合方法,FTOP中有机物质和酚类化合物的浓度降低了97%。因此,所提出的方法能够获得可在其他方法中重复使用的处理过的盐水,并同时浓缩流,例如ADSC。

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