Carbonell-Alcaina Carlos, Soler-Cabezas Jose Luis, Bes-Piá Amparo, Vincent-Vela María Cinta, Mendoza-Roca Jose Antonio, Pastor-Alcañiz Laura, Álvarez-Blanco Silvia
Instituto de Seguridad Industrial, Radiofísica y Medio Ambiental, Universitat Politècnica de València, Camino de Vera s/n, 46022 Valencia, Spain.
Depuración de Aguas del Mediterráneo (DAM), Avenida Benjamín Franklin 21, Parque Tecnológico, 46980 Paterna, Spain.
Membranes (Basel). 2020 Sep 24;10(10):253. doi: 10.3390/membranes10100253.
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.
由于用水需求增加、人口增长以及对水质的监管更加严格,废水管理如今已成为一项重大挑战。食品加工废水尤其难以处理,因为其盐度高且有机物浓度高。这项工作的目的是处理来自油橄榄发酵过程(FTOP)的废水,以便在分离出有机物后将其再利用。本工作提出的工艺由以下基于膜的技术组成:超滤(UF)(UP005,Microdyn Nadir)、正渗透(FO)(Osmen2521,Hydration Technology Innovation)和纳滤(NF)(NF245,陶氏)。实施正渗透工艺是为了降低进入纳滤工艺的盐度,将FTOP用作汲取溶液,同时浓缩城市污水处理厂污泥处理过程中产生的离心液,以获得富含营养物的物流。超滤步骤实现了去除FTOP中50%的化学需氧量。将超滤渗透液泵入正渗透系统,在6.5小时内将厌氧消化污泥离心液(ADSC)的体积减少了三分之一。最后,经正渗透稀释的超滤后的FTOP进行纳滤。纳滤阶段所需的跨膜压力比直接对超滤渗透液进行纳滤所需的压力低40%。通过该集成工艺,FTOP中有机物和酚类化合物的浓度降低了97%。因此,所提出的工艺能够获得可在其他工艺中再利用的处理后盐水,同时浓缩一种物流,如ADSC。