Scientists Map the Hard Physical Limits of Carbon-Capturing Membranes

Carbon dioxide separation has quietly become one of the most consequential chemical operations on the planet. Every tonne of CO2 pulled from a power plant flue stream, stripped from raw biogas, or wrung directly from ambient air costs energy, and the technology that determines how much energy is the humble membrane: a thin, selective barrier that lets carbon dioxide pass while holding back nitrogen, methane, and everything else. Now, a team of researchers at ETH Zürich and the University of Colorado Boulder argues that the field has been grading its best materials against the wrong exam. In a Perspective published in Nature Chemical Engineering, Max Saffer-Meng, Kian P. Lopez, and Anthony P. Straub contend that the classic permeability–selectivity trade-off, which has governed membrane evaluation for decades, is no longer sufficient to judge the next generation of CO2 separation materials.

The trade-off in question dates back to the late twentieth century, when researchers plotting the performance of glassy polymers noticed a stubborn pattern: materials that let CO2 diffuse quickly tended to be poor at rejecting other gases, and highly selective materials tended to be slow. When Lloyd Robeson consolidated these observations into his famous upper-bound plots in 1991 and revisited them in 2008, the resulting curves became the de facto scoreboard for membrane science. Breaking the upper bound became a headline achievement, and entire families of polymers of intrinsic microporosity, thermally rearranged polymers, and mixed-matrix composites have been celebrated for doing exactly that. The new Perspective does not dispute the physics behind these curves, but it insists that the curves answer only one narrow question about one narrow class of materials.

The core of the authors’ argument is that membrane performance is constrained by several distinct physical limits, and the permeability–selectivity trade-off captures only some of them. First, there are inherent upper limits on selectivity itself: no material, however cleverly designed, can distinguish CO2 from other molecules with infinite precision, because sorption and diffusion selectivities are bounded by the thermodynamics and kinetics of the gas–membrane system. Second, permeance, the practical flux per unit area and pressure, does not scale indefinitely with thinning. As membranes approach molecular thicknesses, interfacial resistances, defects, and support-layer limitations begin to dominate, meaning that an ultrathin film cannot simply deliver the permeance predicted by dividing bulk permeability by thickness. Third, operating conditions, most notably CO2 partial pressure, fundamentally alter what a membrane can achieve, sometimes reversing the apparent advantages of one material class over another.

That last point may be the most consequential for real-world deployment. The authors show that materials with high CO2 sorption or reactive affinity, such as facilitated transport membranes built on amines, amino acid salts, ionic liquids, or even enzymes like carbonic anhydrase, shine precisely where the feed gas is dilute and high selectivity is non-negotiable. In direct air capture, where CO2 makes up roughly 420 parts per million of the atmosphere, the driving force for separation is vanishingly small, and only materials that chemically or strongly physically grab CO2 can achieve meaningful capture fractions. But the same high-affinity chemistry becomes a liability at elevated CO2 partial pressures. Carrier saturation, reaction stoichiometry, and plasticization mean that facilitated transport membranes can actually lose permeability and selectivity as the CO2 concentration in the feed rises, a counterintuitive result that simple upper-bound plots cannot predict.

Conversely, the analysis finds that conventional polymers and non-reactive liquids are the materials of choice when CO2 partial pressures are high and very high permeance is required. In natural gas sweetening or pre-combustion capture, where CO2 concentrations can reach tens of percent, the physical solubility and diffusivity of glassy and rubbery polymers provide robust, high-throughput separation without the saturation bottlenecks of reactive carriers. This reframing turns what looks like a materials competition into a matching problem: the best membrane for a given job depends on where that job sits on the partial-pressure axis. A single universal champion material, the authors suggest, is a category error, and research programs that optimize exclusively against the Robeson upper bound may be steering effort toward applications where their materials will never be economically relevant.

The thickness problem deserves particular attention because it sits at the heart of industrial feasibility. Permeance, not permeability, determines the membrane area, and therefore the capital cost, of a full-scale separation plant. The obvious route to high permeance is to make the selective layer thinner, and laboratory reports of films tens of nanometers thick are now common. Yet the Perspective highlights that permeance gains from thinning eventually stall. Surface barriers at the membrane–gas interface, which have been measured even in crystalline zeolites such as silicalite-1, impose a floor on resistance that no amount of thinning can remove. Physical aging in ultrathin glassy films densifies the free volume over time, eroding permeability after fabrication. Pinholes and defects become statistically unavoidable as area scales up, and the porous supports that mechanically hold ultrathin layers add their own resistance. The practical consequence is that permeance targets for post-combustion capture, which earlier techno-economic work by Merkel and colleagues placed in the range of thousands of gas permeation units, remain genuinely difficult even for materials with spectacular intrinsic permeability.

Operating-condition effects extend beyond partial pressure alone. Humidity, for instance, cuts both ways: water can enhance CO2 transport in amine-containing facilitated transport membranes by enabling bicarbonate formation, yet it can swell and degrade ionic-liquid membranes or suppress transport in polybenzimidazoles. Temperature shifts the balance between sorption and diffusion, generally favoring diffusion selectivity at lower temperatures and reactive kinetics at higher ones, and thermal stability limits vary enormously between polymeric, ionic-liquid, and inorganic systems. Pressure ratio, the ratio of feed to permeate CO2 partial pressures, caps the achievable stage cut and purity regardless of how selective the membrane is, a constraint well known to process engineers but often absent from materials-level benchmarking. The authors argue that any credible evaluation framework must fold these variables in from the start, rather than treating them as afterthoughts in a techno-economic analysis performed after the material is already fixed.

Applying this expanded framework yields a set of practical operating windows that map material classes onto industrially relevant separations. For flue-gas carbon capture, with CO2 partial pressures around 0.1 to 0.15 bar, facilitated transport membranes and high-sorption materials hold a genuine edge, provided their stability against humid, oxygen-containing streams can be solved. For biogas upgrading, where CO2 levels near 40 percent meet methane at elevated total pressure, plasticization-resistant polymers and mixed-matrix membranes containing metal–organic framework fillers are better matched to the duty. For direct air capture, the thermodynamic analysis of dilute-gas separation suggests that only membranes combining very high selectivity with high CO2 affinity, potentially including supported ionic liquids and biocatalytic systems, can approach competitive energy footprints, and even then the required membrane areas are daunting. The Perspective also flags potentially disruptive directions: water itself as a separation medium, rubbery organic frameworks aiming at ultrapermeability, and enzymatic liquid membranes that exploit nature’s fastest CO2 conversion chemistry.

What makes the analysis timely is the sheer expansion of the membrane application space. A decade ago, CO2 membranes were largely discussed in the context of natural gas processing and, aspirationally, post-combustion capture. Today, proposals span biogas purification to biomethane, hydrogen purification with CO2 co-capture, and gigatonne-scale direct air capture, each with distinct partial pressures, impurity profiles, and cost sensitivities. Funding agencies and startups alike are pouring resources into novel materials, and the risk identified by Saffer-Meng and colleagues is that of systematic misallocation: brilliant materials optimized for the wrong regime, benchmarked against a curve that cannot see the difference between the regimes. By articulating inherent selectivity ceilings, thickness-dependent permeance constraints, and partial-pressure effects as first-class evaluation criteria, the Perspective offers the field a more honest compass.

The message to membrane scientists is ultimately an enabling one rather than a discouraging one. The upper bound remains a useful map of the diffusion–solubility landscape for glassy polymers, and surpassing it still matters for the applications where those polymers fit. But the frontier of carbon capture now lies in regimes the upper bound never charted: dilute feeds demanding extraordinary selectivity, concentrated feeds demanding plasticization resistance, and ultrathin architectures demanding defect-free scaling. Recognizing the true fundamental limits of each regime, the authors conclude, is the fastest way to direct ingenuity where it can actually move the needle on the economics of separating carbon dioxide from the air, the smokestack, and the digester.

Subject of Research: Fundamental limits of carbon dioxide separation membranes

Article Title: Evaluating the fundamental limits of carbon dioxide separation membranes

Article References: Saffer-Meng, M., Lopez, K. P., & Straub, A. P. (2026). Evaluating the fundamental limits of carbon dioxide separation membranes. Nature Chemical Engineering. https://doi.org/10.1038/s44286-026-00441-9

Image Credits: AI Generated

DOI: 10.1038/s44286-026-00441-9

Keywords: carbon capture, CO2 separation, membranes, Robeson upper bound, facilitated transport, direct air capture, flue gas, biogas upgrading, ionic liquids, permeance, selectivity, chemical engineering