Rochow Maria F, Cassady Harrison J, Hickner Michael A
Department of Material Science and Engineering, Penn State, University Park, Pennsylvania 16802-1503, United States.
Department of Chemical Engineering, Penn State, University Park, Pennsylvania 16802-1503, United States.
ACS Appl Polym Mater. 2025 Apr 17;7(9):5456-5464. doi: 10.1021/acsapm.5c00148. eCollection 2025 May 9.
Bipolar membranes (BPMs) are a unique construction of ion exchange membranes with anion exchange and cation exchange layers in series. Due to the unique transport processes in BPMs, they are becoming an increasingly attractive option for many electrochemical devices, especially in water electrolysis and carbon dioxide reduction. However, because a large number of anion and cation exchange membranes are available, it can be difficult to select the layers for BPM fabrication, particularly when targeting specific properties for use in a device. In this study, a survey of nine anion and nine cation exchange membranes was conducted to assess their steady-state ion transport properties. The primary application of this work is seawater electrolysis; therefore, measurements of salt flux and area resistance in 0.5 mol/L sodium chloride solutions were performed. These measurements displayed a trade-off behavior, with membranes displaying higher area resistance and having a lower salt flux. Conversely, membranes with lower area resistance had a higher salt flux. From these individual membrane results, a methodology was formulated to select component membranes for BPM fabrication, primarily considering their transport characteristics. Three BPMs were fabricated using this methodology. A model was developed to integrate the parameters and ion transport properties measured from individual membranes to predict salt flux and area resistance values for a BPM. Values produced from the model were then compared with experimental salt flux and area resistance BPM measurements. Both the model and experimental salt flux and area resistance BPMs exhibited an area resistance-flux trade-off, like that of the component membranes.
双极膜(BPMs)是一种独特的离子交换膜结构,由串联的阴离子交换层和阳离子交换层组成。由于双极膜中独特的传输过程,它们在许多电化学装置中越来越具有吸引力,特别是在水电解和二氧化碳还原方面。然而,由于有大量的阴离子和阳离子交换膜可供选择,为双极膜制造选择合适的膜层可能会很困难,尤其是当目标是针对特定装置性能时。在本研究中,对九种阴离子交换膜和九种阳离子交换膜进行了调查,以评估它们的稳态离子传输性能。这项工作的主要应用是海水电解;因此,在0.5mol/L氯化钠溶液中进行了盐通量和面积电阻的测量。这些测量结果显示出一种权衡行为,即膜的面积电阻较高时盐通量较低。相反,面积电阻较低的膜盐通量较高。根据这些单个膜的结果,制定了一种方法来选择用于制造双极膜的组件膜,主要考虑它们的传输特性。使用该方法制备了三种双极膜。开发了一个模型,将从单个膜测量得到的参数和离子传输性能整合起来,以预测双极膜的盐通量和面积电阻值。然后将模型得出的值与双极膜的实验盐通量和面积电阻测量值进行比较。模型以及双极膜的实验盐通量和面积电阻都表现出面积电阻 - 通量的权衡,类似于组件膜的情况。