Pressure-driven distillation using air-trapping membranes for fast and selective water purification

High Pressure Resistance in Omniphobic Distillation Membranes with Re-entrant Nanostructures

We developed pressure-resistant omniphobic membranes that enable stable distillation of low-surface-tension liquids at applied pressures exceeding 15 bar. Membranes were synthesized by grafting re-entrant nanostructures onto porous alumina membranes, followed by hydrophobic modification. The membranes exhibited a high liquid entry pressure of 36.2 bar with water and withstood an applied pressure up to 15.5 bar with a low-surface-tension 15 wt % ethanol-water mixture. Simulations revealed that the enhanced wetting resistance is due to the presence of re-entrant structures, which facilitated a 220% increase in wetting pressure for the low-surface-tension liquid compared to a control membrane with cylindrical pores. We further demonstrated stable pressure-driven distillation of low-surface-tension liquids, achieving higher than 97% salt rejection. This work is the first demonstration of distillation membranes operating with low-surface-tension liquids under high applied pressures and provides critical validation of wettability theory under extreme pressures.

Fluorine-Free Nanofiber/Network Membranes with Interconnected Tortuous Channels for High-Performance Liquid-Repellency and Breathability

The excessive use of fluoride in fibrous membranes poses significant bioaccumulative threats to the environment and human health. However, most existing membranes used in protective clothing and desalination systems show high fluorine dependence and inevitable trade-offs between liquid repellency and breathability. Herein, fluorine-free bonded scaffolded nanofiber/network membranes are developed using the electro-coating-netting technique to achieve high-performance liquid-repellency and breathability. By manipulating the stretching of electrospun jets and the polarization of electrets, rough and electrostatic wetting nanofibers are obtained as scaffolds, on which long-chain alkyl precursors are coated to assemble 2D networks consisting of nanowires with diameters of ∼42 nm and bonding points. The resultant fluorine-free membranes exhibit small pore sizes of ∼460 nm, highly interconnected tortuous channels, a water contact angle of ∼138°, and elastic elongation up to 300%, thereby providing both high-performance liquid repellency (125 kPa) and vapor permeability (4206 g m-2 d-1), making them effective for use in protective clothing and desalination. This work could inspire innovative design of ecofriendly nanofibrous materials for high-performance filtration and separation.

Permeability-selectivity trade-off for a universal leaky channel inspired by mobula filters

Mobula rays have evolved leaf-shaped filter structures to separate food particles from seawater, which function similarly to industrial cross-flow filters. Unlike cross-flow filtration, where permeability and selectivity are rationally designed following trade-off analyses, the driving forces underlying the evolution of mobula filter geometry have remained elusive. To bridge the principles of cross-flow and mobula filtration, we establish a universal framework for the permeability-selectivity trade-off in a leaky channel inspired by mobula filters, where permeability and selectivity are characterized by the pore-scale leaking rate and the cut-off particle size, respectively. Beyond the classic pore-flow regime in cross-flow filtration, we reveal transition and vortex regimes pertinent to mobula filtration. Combining theory, physical experiments, and simulations, we present distinct features of water permeability and particle selectivity across the three regimes. In particular, we identify an unreported 1/2-scaling law for the leaking rate in the vortex regime. We conclude by demonstrating that mobula filters strike an elegant balance between permeability and selectivity, which enables mobula rays to simultaneously satisfy biological requirements for breathing and filter feeding. By integrating cross-flow and mobula filtration into a universal framework, our findings provide fundamental insights into the physical constraints and evolutionary pressures associated with biological filtration geometries and lay the foundation for developing mobula-inspired filtration in industry.

Ultra-high freshwater production in multistage solar membrane distillation via waste heat injection to condenser

Passive solar membrane distillation (MD) is an emerging technology to alleviate water scarcity. Recently, its performance has been enhanced by multistage design, though the gains are marginal due to constrained temperature and vapor pressure gradients across the device. This makes condenser cooling enhancement a questionable choice. We argue that condenser heating could suppress the marginal effect of multistage solar MD by unlocking the moisture transport limit in all distillation stages. Here, we propose a stage temperature boosting (STB) concept that directs low-temperature heat to the condensers in the last stages, enhancing moisture transport across all stages. Through STB in the last two stages with a heat flux of 250 W m-2, a stage-averaged distillation flux of 1.13 L m-2 h-1 S-1 was demonstrated using an 8-stage MD device under one-sun illumination. This represents an 88% enhancement over the state-of-the-art 10-stage solar MD devices. More notably, our analysis indicates that 16-stage STB-MD devices driven by solar energy and waste heat can effectively compete with existing photovoltaic reverse osmosis (PV-RO) systems, potentially elevating freshwater production with low-temperature heat sources.

Antifouling binary liquid-infused membranes for biological sample pretreatment

Hydrophobic membranes infused with mixed solvents including a low polar solvent and a specific solvent can efficiently separate analytes from blood upon applying a voltage. In contrast, membranes infused with a specific solvent alone show significantly reduced separation efficiencies for blood samples. Infusion of a low polar solvent is of importance for achieving antifouling ability of membranes for biological sample pretreatment.

Unifying the Conversation: Membrane Separation Performance in Energy, Water, and Industrial Applications

Dense polymer membranes enable a diverse range of separations and clean energy technologies, including gas separation, water treatment, and renewable fuel production or conversion. The transport of small molecular and ionic solutes in the majority of these membranes is described by the same solution-diffusion mechanism, yet a comparison of membrane separation performance across applications is rare. A better understanding of how structure-property relationships and driving forces compare among applications would drive innovation in membrane development by identifying opportunities for cross-disciplinary knowledge transfer. Here, we aim to inspire such cross-pollination by evaluating the selectivity and electrochemical driving forces for 29 separations across nine different applications using a common framework grounded in the physicochemical characteristics of the permeating and rejected solutes. Our analysis shows that highly selective membranes usually exhibit high solute rejection, rather than fast solute permeation, and often exploit contrasts in the size and charge of solutes rather than a nonelectrostatic chemical property, polarizability. We also highlight the power of selective driving forces (e.g., the fact that applied electric potential acts on charged solutes but not on neutral ones) to enable effective separation processes, even when the membrane itself has poor selectivity. We conclude by proposing several research opportunities that are likely to impact multiple areas of membrane science. The high-level perspective of membrane separation across fields presented herein aims to promote cross-pollination and innovation by enabling comparisons of solute transport and driving forces among membrane separation applications.