Membrane capacitive deionization (MCDI) has emerged as an effective and energy efficient desalination technology for treating brackish water streams used in numerous industrial processes. Most material research studies on MCDI focus on improving the porous electrodes or using flowing electrode architectures, and little emphasis is given to the rationale design of ion-exchange membranes (IEMs) for MCDI. In this work, the ionic conductivity, permselectivity, and thickness for three different IEM chemistries (polyaliphatic, poly(arylene ether), and perfluorinated) were correlated to MCDI performance attributes: energy expended per ion removed, salt removal efficiency, and Coulombic efficiency. A 5-to 10-fold reduction in area specific resistance, which accounts for thickness and ionic conductivity, with unconventional perfluorinated and poly(arylene ether) IEMs reduced the energy expended per ion removed in MCDI by a factor of 2 when compared to conventional electrodialysis IEMs. In situ electrochemical impedance spectroscopy substantiated that thinner membranes with higher ionic conductivity helped in the reduction of energy expended per ion removed (more than 50%). Finally, the lower than 100% Coulombic efficiency is ascribed to carbon corrosion of the porous electrodes highlighting that further improvements in MCDI do not just necessitate more appropriate membranes but corrosion resilient electrodes.
Thermally regenerative batteries (TRBs) is an emerging platform for extracting electrical energy from low-grade waste heat (T < 130 °C). TRBs using an ammonia-copper redox couple can store waste-heat energy in a chemical form that can be later discharged to electrical energy upon demand. Previous thermally regenerative ammonia battery (TRAB) demonstrations suffered from poor heat to electrical energy conversion efficiency when benchmarked against thermoelectric generators (TEGs). In this work, we report the highest power density to date for a TRAB (280 W m −2 at 55 °C) with a 5.7× improvement in power density over conventional TRAB designs. Notably, the TRAB was configured similar to a redox flow battery setup, which is termed here an ammonia flow battery (AFB). The substantial improvement in the AFB power density translated to thermal efficiency (η th ) values as high as 2.99% and 37.9% relative to the Carnot efficiency (η th/C ). These values correspond to an 87.6% improvement in η th value over conventional TRAB designs and the highest reported η th/C for low-grade waste heat recovery using TRABs. The excellent performance of the AFB was ascribed to a zero gap design, deploying a low-resistant, inexpensive anion exchange membrane (AEM), and implementing a copper ion selective ionomer coating on the copper mesh electrodes. The high-power AFB in this report represents a significant milestone in harvesting low-grade waste heat.
Microbial desalination cell (MDC) is a bioelectrochemical system capable of oxidizing organics, generating electricity, while reducing the salinity content of brine streams. As it is designed, anion and cation exchange membranes play an important role on the selective removal of ions from the desalination chamber. In this work, sulfonated sodium (Na) poly(ether ether ketone) (SPEEK) cation exchange membranes (CEM) were tested in combination with quaternary ammonium chloride poly(2,6-dimethyl 1,4-phenylene oxide) (QAPPO) anion exchange membrane (AEM). Non-patterned and patterned (varying topographical features) CEMs were investigated and assessed in this work. The results were contrasted against a commercially available CEM. This work used real seawater from the Pacific Ocean in the desalination chamber. The results displayed a high desalination rate and power generation for all the membranes, with a maximum of 78.6±2.0% in salinity reduction and 235±7mWm in power generation for the MDCs with the SPEEK CEM. Desalination rate and power generation achieved are higher with synthesized SPEEK membranes when compared with an available commercial CEM. An optimized combination of these types of membranes substantially improves the performances of MDC, making the system more suitable for real applications.
Quaternary ammonium poly(2,6-dimethyl 1,4-phenylene oxide) (QAPPO) anion exchange membranes (AEMs) with topographically patterned surfaces were assessed in a microbial desalination cell (MDC) system. The MDC results with these QAPPO AEMs were benchmarked against a commercially available AEM. The MDC with the non-patterned QAPPO AEM (Q1) displayed the best desalination rate (a reduction of salinity by 53 ± 2.7%) and power generation (189 ± 5 mW m − 2 ) when compared against the commercially available AEM and the patterned AEMs. The enhanced performance with the Q1 AEM was attributed to its higher ionic conductivity and smaller thickness leading to a reduced area specific resistance. It is important to note that Real Pacific Ocean seawater and activated sludge were used into the desalination chamber and anode chamber respectively for the MDC – which mimicked realistic conditions. Although the non-patterned QAPPO AEM displayed better performance over the patterned QAPPO AEMs, it was observed that the anodic overpotential was smaller when the MDCs featured QAPPO AEMs with larger lateral feature sizes. The results from this study have important implications for the continuous improvements necessary for developing cheaper and better performing membranes in order to optimize the MDC.
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