Kalafatakis Stavros, Zarebska Agata, Lange Lene, Hélix-Nielsen Claus, Skiadas Ioannis V, Gavala Hariklia N
Technical University of Denmark (DTU), Department of Chemical and Biochemical Engineering, Søltofts Plads 229, 2800 Kgs. Lyngby, Denmark.
Technical University of Denmark (DTU), Department of Environmental Engineering, Miljøvej 113, 2800 Kgs. Lyngby, Denmark.
Membranes (Basel). 2020 Oct 27;10(11):307. doi: 10.3390/membranes10110307.
Forward Osmosis (FO) is a promising technology that can offer sustainable solutions in the biorefinery wastewater and desalination fields, via low energy water recovery. However, microbial biomass and organic matter accumulation on membrane surfaces can hinder the water recovery and potentially lead to total membrane blockage. Biofouling development is a rather complex process and can be affected by several factors such as nutrient availability, chemical composition of the solutions, and hydrodynamic conditions. Therefore, operational parameters like cross-flow velocity and pH of the filtration solution have been proposed as effective biofouling mitigation strategies. Nevertheless, most of the studies have been conducted with the use of rather simple solutions. As a result, biofouling mitigation practices based on such studies might not be as effective when applying complex industrial mixtures. In the present study, the effect of cross-flow velocity, pH, and cell concentration of the feed solution was investigated, with the use of complex solutions during FO separation. Specifically, fermentation effluent and crude glycerol were used as a feed and draw solution, respectively, with the purpose of recirculating water by using FO alone. The effect of the abovementioned parameters on (i) ATP accumulation, (ii) organic foulant deposition, (iii) total water recovery, (iv) reverse glycerol flux, and (v) process butanol rejection has been studied. The main findings of the present study suggest that significant reduction of biofouling can be achieved as a combined effect of high-cross flow velocity and low feed solution pH. Furthermore, cell removal from the feed solution prior filtration may further assist the reduction of membrane blockage. These results may shed light on the challenging, but promising field of FO process dealing with complex industrial solutions.
正向渗透(FO)是一项很有前景的技术,它可以通过低能耗水回收为生物精炼废水和海水淡化领域提供可持续的解决方案。然而,微生物生物质和有机物在膜表面的积累会阻碍水的回收,并可能导致膜完全堵塞。生物污垢的形成是一个相当复杂的过程,会受到多种因素的影响,如营养物质的可用性、溶液的化学成分和流体动力学条件。因此,已提出诸如错流速度和过滤溶液pH值等操作参数作为有效的生物污垢缓解策略。然而,大多数研究都是使用相当简单的溶液进行的。因此,基于此类研究的生物污垢缓解措施在应用于复杂的工业混合物时可能效果不佳。在本研究中,在FO分离过程中使用复杂溶液,研究了错流速度、pH值和进料溶液细胞浓度的影响。具体而言,分别使用发酵废水和粗甘油作为进料溶液和汲取溶液,目的是仅通过FO来循环水。研究了上述参数对(i)ATP积累、(ii)有机污垢沉积、(iii)总水回收率、(iv)反向甘油通量和(v)过程丁醇截留率的影响。本研究的主要发现表明,高错流速度和低进料溶液pH值的综合作用可显著减少生物污垢。此外,在过滤前从进料溶液中去除细胞可能进一步有助于减少膜堵塞。这些结果可能为处理复杂工业溶液的FO过程这一具有挑战性但前景广阔的领域提供启示。