Tunable molecular separation by nanoporous membranes

Abstract

Metal-organic frameworks offer tremendous potential for efficient separation of molecular mixtures. Different pore sizes and suitable functionalizations of the framework allow for an adjustment of the static selectivity. Here we report membranes which offer dynamic control of the selectivity by remote signals, thus enabling a continuous adjustment of the permeate flux. This is realized by assembling linkers containing photoresponsive azobenzene-side-groups into monolithic, crystalline membranes of metal-organic frameworks. The azobenzene moieties can be switched from the trans to the cis configuration and vice versa by irradiation with ultraviolet or visible light, resulting in a substantial modification of the membrane permeability and separation factor. The precise control of the cis:trans azobenzene ratio, for example, by controlled irradiation times or by simultaneous irradiation with ultraviolet and visible light, enables the continuous tuning of the separation. For hydrogen:carbon-dioxide, the separation factor of this smart membrane can be steplessly adjusted between 3 and 8.

ARTICLE

Received 5 Sep 2016 | Accepted 7 Nov 2016 | Published 20 Dec 2016

Zhengbang Wang1,*, Alexander Knebel2,*, Sylvain Grosjean3, Danny Wagner4, Stefan Brase3,4,5, Christof Wll1, Jrgen Caro2 & Lars Heinke1

Metal-organic frameworks offer tremendous potential for efcient separation of molecular mixtures. Different pore sizes and suitable functionalizations of the framework allow for an adjustment of the static selectivity. Here we report membranes which offer dynamic control of the selectivity by remote signals, thus enabling a continuous adjustment of the permeate ux. This is realized by assembling linkers containing photoresponsive azobenzene-side-groups into monolithic, crystalline membranes of metal-organic frameworks. The azobenzene moieties can be switched from the trans to the cis conguration and vice versa by irradiation with ultraviolet or visible light, resulting in a substantial modication of the membrane permeability and separation factor. The precise control of the cis:trans azobenzene ratio, for example, by controlled irradiation times or by simultaneous irradiation with ultraviolet and visible light, enables the continuous tuning of the separation. For hydrogen:carbon-dioxide, the separation factor of this smart membrane can be steplessly adjusted between 3 and 8.

DOI: 10.1038/ncomms13872 OPEN

Tunable molecular separation by nanoporous membranes

1 Institute of Functional Interfaces (IFG), Karlsruhe Institute of Technology (KIT), Hermann-von-Helmholtz-Platz 1, 76344 Eggenstein-Leopoldshafen, Germany. 2 Institute for Physical Chemistry and Electrochemistry, Leibniz University Hanover, Callinstra 3a, 30167 Hannover, Germany.

3 Soft Matter Synthesis Lab, Institute of Biological Interfaces 3 (IBG 3), Karlsruhe Institute of Technology (KIT), Hermann-von-Helmholtz-Platz 1, 76344 Eggenstein-Leopoldshafen, Germany. 4 Institute of Organic Chemistry (IOC), Karlsruhe Institute of Technology (KIT), Fritz-Haber-Weg 6, 76131 Karlsruhe, Germany. 5 Institute of Toxicology and Genetics (ITG), Karlsruhe Institute of Technology (KIT), Hermann-von-Helmholtz-Platz 1, D-76344 Eggenstein-Leopoldshafen, Germany. * These authors contributed equally to this work. Correspondence and requests for materials should be addressed to A.K. (email: mailto:[email protected]

Web End [email protected] ) or to L.H. (email: mailto:[email protected]

Web End [email protected] ).

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Many sustainable applications require an efcient and energy-saving separation of molecular mixtures1. In this context, membrane technologies hold substantial

potential for the separation of gas or liquid mixtures, since they offer an economic, energy-saving and ecological alternative to energy-intensive distillation or cryogenic separations. To reach high efciencies, compelling research efforts are undertaken to develop novel materials allowing the fabrication of membranes with high permeation uxes and high molecular separation factors. Ultrathin polymer2 and porous carbon3 membranes as well as two-dimensional materials, like graphene and graphene oxide4,5, are considered to be auspicious materials in this context, since they offer high permeation uxes, chemical stability, extensive mechanical strength and exibility. However, a remaining major challenge is the precise control over the chemical functionality and over the pore size. Recently, metal-organic frameworks (MOFs)6, crystalline solids composed of metal nodes connected by organic linker molecules, demonstrated large potential for membrane separation processes712. MOFs possess an abundance of unique properties like well-dened, periodic nanoporous structures, large specic surface areas and large structural and chemical variety, with more than 20,000 different MOF structures published before 2013 (ref. 6). Furthermore, the structure or chemical functionality of MOFs can be modied by different pre- and post-synthetic methods13, which allow to further adjust the specic properties of these porous materials.

Of particular interest with respect to membrane fabrication is remote control, that is, the ability to switch crucial membrane parameters, like permeance or selectivity, by external stimuli without direct contact. Integrating such smart membranes into separation systems is expected to lead to a major break-through in overall performance. Light is a particularly simple, handy and (usually) non-invasive signal. Thus, photosensitive molecules, which undergo reversible isomerization when irradiated with light of a certain wavelength, attract a lot of attention1416. Photoisomerization processes are typically very fast and

can be repeated many times. By incorporating photoswitchable molecular groups in molecular compounds like polymers and liquid crystals, some properties of these materials can be modied by illumination. Photoswitchable azobenzene-containing polymers and liquid crystals have been used as actuators17,18 and light-driven motors19. Furthermore, photoswitchable molecular scaffolds20 and gel assemblies21 were realized utilising azobenzene photoisomerization. Also, for MOFs in the form of powders or thin lms, photoswitchable moieties2224 were used to demonstrate the remote-control of the MOF properties like colour25, release2628 and adsorption2933 of the guest molecules, in particular of CO2 (refs 32,33). While in most cases illumination with ultraviolet-light was needed, linker molecules that can be switched with visible light were used for the MOF preparation recently34.

Here, we describe the design of a nanoporous, photoswitchable MOF membrane, where the azobenzene moieties are incorporated as side groups into the framework. By controlling the isomerization state of the photosensitive groups by light, the ux and the separation factor of a molecular, gaseous mixture permeating the membrane can be switched. In addition to varying the permeability, the separation factor (also referred to as (perm-)selectivity) can be continuously tuned by adjusting the ratio of the trans and cis isomers of the photochromic moieties. As a result, the molecular composition of the permeate ux can be precisely tuned in a fully remote-controlled way, see Fig. 1.

ResultsPhotoswitchable SURMOF lms. The membranes are fabricated by growing MOF thin lms in a layer-by-layer fashion, employing liquid-phase epitaxy by alternatively immersing the sample in solutions containing the MOF components, that is, in (separate) solutions of the metal nodes and of the organic linker molecules. This technique yields monolithic, crystalline, continuous MOF lms, referred to as surface-mounted MOFs (SURMOFs)3538. The prepared SURMOF lms have a pillared-layer structure of type Cu2(AzoBPDC)2(AzoBiPyB) (Fig. 2;

AzoBPDC: 2-phenyldiazenyl-4,40-biphenyldicarboxylic acid26, and AzoBiPyB: (E)-4,40-(2-(phenyldiazenyl)-1,4-phenylene) dipyridine (or dipyridylazobenzene)30. The samples used in this study were prepared by 90 (or 60) cycles of immersing the sample in ethanolic 1 mM copper(II)acetate solution and in ethanolic0.1 mM AzoBiPyB and 0.1 mM AzoBPDC solution at 60 C. Uptake experiments with butanol as guest molecule using a quartz crystal microbalance39,40 indicate that the used MOF structure, that is, Cu2(AzoBPDC)2(AzoBiPyB) with three azobenzene moieties per unit cell, results in large effects of the trans-cis switching, see Supplementary Fig. 1. The SURMOF lms were prepared on quartz glass and on gold thin lms on silicon supports for ultravioletvis (UV-vis) and infrared reection absorption spectroscopy (IRRAS), respectively. For the membrane separation, the SURMOF lms were prepared on asymmetric mesoporous aluminium oxide supports, which have a pore size of 70 nm on the top surface. Before the synthesis, the gold substrates were functionalized by 11-mercapto-1-undecanol (MUD) self-assembled monolayers (SAMs), while the quartz and porous aluminium oxide substrates were functionalized by oxygen plasma treatment41.

From the IRRAS (Fig. 2b) and ultravioletvis spectra (Supplementary Fig. 2), it is clearly visible that the azobenzene (or phenyldiazenyl) side groups in the MOF can be switched by irradiation with light of 365 nm from trans (E) to cis (Z) and vice versa with light of 455 nm. The X-ray diffractograms of the SURMOF (Fig. 2c) indicate that the crystalline MOF (lattice) structure is not affected by the irradiation with ultraviolet or

Photoswitchable MOF membrane

Porous -Al 2O 3support

Continuosly tunning of permeate composition

Figure 1 | Switchable membrane separation. Schematic illustration of tunable, remote-controllable molecular selectivity by a photoswitchable MOF membrane. The molecular feed mixture (left-hand side), where the molecules are depicted in red and blue, is separated by the nanoporous membrane. The molecular separation factor, giving the composition of the permeation ux (right-hand side), can be continuously tuned by light irradiation.

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Figure 2 | Photoswitchable SURMOFs of type Cu2(AzoBPDC)2(AzoBiPyB). (a) The structure of Cu2(AzoBPDC)2(AzoBiPyB) with the azobenzene groups in the (basic) trans state, left, and in the cis state, right. The photoisomerization from trans to cis is performed by irradiation with ultraviolet-light of 365 nm, while the cis-to-trans isomerization is performed by irradiation with blue light of 455 nm. (Different view points of the MOF structure are shown in Supplementary Fig. 3.) (b) Infrared spectra of the Cu2(AzoBPDC)2(AzoBiPyB) SURMOF in the pristine trans state (black), after ultraviolet irradiation with light of 365 nm (red) and after irradiation with visible light of 455 nm (blue). The inset shows the magnication of the trans and cis azobenzene bands at about 720 and 730 cm 1, respectively. An infrared spectrum with a larger range is shown in Supplementary Fig. 4. (c) Out-of-plane X-ray diffractogram of Cu2(AzoBPDC)2(AzoBiPyB) SURMOF before (black) and after (red) ultraviolet irradiation.

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Figure 3 | Photoswitching of the SURMOF lms. Amount of trans azobenzene (black triangles) and cis azobenzene (red spheres) of the Cu2(AzoBPDC)2(AzoBiPyB) SURMOF. (a) The sample is initially in the (100%) trans state and is irradiated with 365 nm. (b) The sample is initially in the cis state (that is, 63% cis) and is irradiated with 455 nm. The insets show the infrared trans azobenzene peak at 720 cm 1 during the irradiation with 365 and 455 nm, respectively. (c) The sample is simultaneously irradiated with light of 365 and 455 nm. The irradiation time of each point is 30 min, resulting in a photostationary state. The ratio of cis azobenzene, determined from the infrared peak at 720 cm 1, is shown as a function of intensity of 365 nm relative to the total light intensity (365 and 455 nm). The light intensities are (roughly) adjusted by the potentiometers of the LEDs.

visible light, this means, by the photoisomerization of the azobenzene-side-groups.

For a detailed understanding of the photoswitching in the MOF lm, the photoisomerization during irradiation with ultraviolet or visible light or their mixture was studied by using IRRAS. By analysing the intensity of the infrared vibrational band at about 720 cm 1, which can be assigned to trans azobenzene42, the percentage of trans azobenzene and therefore of cis

azobenzene in the MOF structure was determined. This band may be assigned to the g(CH) and t(ring) vibration of the trans azobenzene side group, which, because of the bonding to the framework, is red shifted in comparison to the vibration band of the isolated azobenzene43,44.

The maximum yield of cis azobenzene, this means, the photo-stationary state under irradiation by light of 365 nm wavelength, was determined to be B63%, Fig. 3a. The percentage of cis and

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a

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-Al2O3 support

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Figure 4 | Membrane separation setup. (a) Sketch of the setup for the photoswitchable membrane permeation experiments. The feed-retentate gas ow is above the membrane, while the sweep-permeate gas ow is below the membrane. A ber-coupled LED is used for in situ irradiation of the SURMOF-covered top-side of the alumina membrane. (b) SEM cross-section image of the SURMOF membrane on the mesoporous a-alumina support.

A dense SURMOF layer with a thickness of roughly 2 mm is observed. The length of the white scale bar is 5 mm.

9

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trans isomers can be adjusted by controlling the illumination time of the LED light with either 365 or 455 nm wavelength, see Fig. 3a,b. Moreover, a given cis:trans azobenzene ratio can also be achieved by simultaneously irradiating the SURMOF lm with light of 365 and 455 nm, resulting in a steady state with equal rates of simultaneous trans-to-cis and cis-to-trans isomerizations. By adjusting the intensities of the respective LEDs with 365 or 455 nm wavelengths, a well-dened cis:trans ratio can be adjusted, see Fig. 3c. It should be noted that cis azobenzene can undergo thermal relaxation back to trans azobenzene with a thermal relaxation time of about 20 days at room temperature42. Therefore, the isomerization state of the photoswitchable SURMOF can be considered as stable in the dark, this means, without light irradiation, for the duration of the experiment (approximately a few hours).

Tunable and remote-controllable membrane permeation. The investigation of the photoswitchable membrane permeation was executed by growing Cu2(AzoBPDC)2(AzoBiPyB) SURMOFs on mesoporous aluminium oxide supports. As shown by the SEM image in Fig. 4b, a continuous, dense and pinhole-free SURMOF lm with a thickness of about 2 mm was formed on the mesoporous support. The X-ray diffractograms (Supplementary Fig. 5) verify the crystalline structure of the Cu2(AzoBPDC)2 (AzoBiPyB) SURMOF on the mesoporous support. For performing the membrane separation measurements, a WickeKallenbach setup45 with an optical bre enabling the in situ irradiation of the MOF membrane was designed and built (Fig. 4a). This set-up allows to photoswitch the Cu2(AzoBPDC)2(AzoBiPyB) SURMOF membrane, and to adjust the cis:trans azobenzene ratio during the membrane separation experiments. Here, the molecular separations of two different binary mixtures, H2:CO2 (pre-combustion mixtures)

and N2:CO2 (post-combustion mixtures), were studied.

The membrane permeances and separation factors of hydrogen and carbon dioxide from the 50%:50% feed mixture are shown in Fig. 5a. The high separation factor indicates the absence of defects and pinholes in the membrane. While the permeation of hydrogen decreases only slightly, the permeation of carbon dioxide signicantly decreases on switching the azobenzene-containing MOF membrane from trans to cis. The CO2 permeance can be switched between B4 and 10 10 8 mol s 1

m 2 Pa 1. The molecular H2:CO2 separation factor increases

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Figure 5 | Photoswitchable membrane separation. The separation of H2:CO2 and N2:CO2 mixtures is shown in (a,b), respectively. The membrane is irradiated by light of 365 and 455 nm for 5 min each. The permeances of H2 and CO2 (a), as well as N2 and CO2 (b) are shown as black solid squares and black open squares, respectively, with the logarithmic scale on the right-hand side. The molecular selectivities (or separation factors) are shown as red spheres with the scale on the left-hand side.

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Figure 6 | Tuning the H2:CO2 separation factor by adjusting the cis:trans azobenzene ratio. (a) The Cu2(AzoBPDC)2(AzoBiPyB) membrane, which is initially in the trans state, is irradiated with ultraviolet-light for time intervals of 100 and 200 s, resulting in an increase of the H2:CO2 selectivity.(b) The membrane is initially in the cis state and is irradiated with 455 nm for time intervals of 30 and 50 s. (c) Correlation of the H2:CO2 separation factor with the ratio of cis azobenzene. The grey triangle and black spheres represent the data from gure (a,b), respectively; the correlation to the cis azobenzene ratio results from the comparison with the IRRAS data, see Supplementary Fig. 6.

from 3.0 in the trans state (100% trans, 0% cis) to about 8.0 in the cis state (37% trans, 63% cis). After irradiation with 455 nm, this means, the azobenzene-side-groups are switched back to the basic trans state, the initial permeances and the separation factor of 3 are attained. Five consecutive cycles of irradiation with 365 and 455 nm, this means, switching between the trans and the cis state, were performed. It was found that the switching of the membrane permeance and separation factor are fully reversible and, in addition, shows no sign of bleaching.

In a previous study with alkanes, alcohols and diols as guest molecules, it could be shown that the difference of the uptake by the azobenzene-containing MOF in the cis and in the trans state is caused by the switching of the azobenzene dipole moment, which amounts to 0 Debye in trans and 3 Debye in cis, and the dipoledipole interaction with the guest molecules39. Thus, we may assume that the molecular mechanism resulting in the switching of the molecular separation is related to the different interaction of the hydrogen and carbon dioxide multipole moments with the cis- or trans-MOF, rather than a pore size effect or steric hindrance. Indeed, the dipole moment of the cis azobenzene is expected to result in a higher attractive interaction with the fairly strong quadrupole-moment of carbon dioxide, thus slowing down the carbon dioxide diffusion, while the interaction with hydrogen is not affected by the trans-cis switching. As a result, the different impact of the trans-cis switching leads to the switching of the H2:CO2 separation factor.

A reversible switching of the molecular selectivity is also observed for the separation of the N2:CO2 mixture, where the selectivity increases from 5.5 to 8.5 when switching from trans to cis, see Fig. 5b. While the carbon dioxide permeation signicantly decreases on trans-to-cis isomerization, the nitrogen permeation is hardly affected. The observed permeation selectivity of nitrogen over carbon dioxide is characteristic for wide-pore

MOF/zeolite membranes with an adsorption controlled separation mechanism4648, whereas narrow-pore MOF/zeolite membranes show a preferred carbon dioxide (critical diameter3.3 ) permeation in comparison with nitrogen (3.6 ) because of a diffusion-controlled molecular sieve mechanism45,49,50.

A profound feature of the photoswitchable membrane is that the impressive (OnOff) switching of the separation factors (between membranes with minimum and maximum cis ratios) can be combined with the option of ne-tuning the cis azobenzene ratios. The H2:CO2 separation factor of the membrane in the trans state can be increased in arbitrary steps until the maximum separation factor is reached by irradiation with ultraviolet-light for certain time, Fig. 6a. On the other hand, the separation factor of the cis membrane can be decreased in arbitrary steps by irradiation with 455 nm, Fig. 6b. Thus, the separation factor can not only be switched between the minimum and maximum values, that is, 3.0 for 0% cis azobenzene and 8.0 for 63% cis azobenzene, but also each value in between can be realized by choosing appropriate irradiation times, that is, by adjusting the cis azobenzene ratio. The continuous tuning of the cis azobenzene ratio by controlled irradiation times with ultraviolet or visible light (Fig. 3) thus allows for a continuous tuning of the separation factor (Fig. 6). A correlation of the membrane selectivity with the cis-azobenzene ratio from the IRRAS data are shown in Fig. 6c. Because of the slow thermal isomerization of the azobenzene groups, the separation factor belonging to a mixed cis:trans state, once adjusted, is stable in the dark for the duration of the experiments.

DiscussionThe ratio of the azobenzene isomers can also be controlled by adjusting the relative intensities of the multi-component light

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irradiation with ultraviolet and visible light (Fig. 3c). For instance, a H2:CO2 selectivity of 4.5 is reached for a cis ratio of about 20%.

This ratio can be adjusted by irradiating the (100%) trans membrane with 365 nm for about 500 s (Fig. 6a), by irradiating the (63%) cis membrane with 455 nm for about 120 s (Fig. 6b) or by simultaneously irradiating the sample with 365 and 455 nm with an intensity ratio of about 20%:80% (Fig. 3c).

By increasing the cis ratio, that is, by increasing the irradiation time with ultraviolet-light or by increasing the relative ultraviolet intensity, the separation factor is increased. Here, the maximum ratio of cis azobenzene is about 63%, resulting in the highest separation factor of about 8.0. It can be assumed that even higher cis:trans isomerization ratios, for example, enabled by functionalized azobenzene moieties51, would result in higher switching yields and would enlarge the tunable separation factor range.

The potential of the tunable membrane is demonstrated by controlling the molecular composition of the H2:CO2 permeate ux and, therewith, controlling the ammability and the safety of this pre-combustion mixture when mixed with air or oxygen. When the permeate ux is mixed with air in a ratio 1:20, the resulting gas ow through the membrane in the trans state has a hydrogen content of 3.7%, while the ux through the cis membrane has a hydrogen content of 4.4%. Since the ammability limit of hydrogen in air is 4.0% (ref. 52), the photoswitchable membrane in the cis state results in a ammable gas mixture and the trans membrane in a non-ammable gas mixture. When the permeate ux is mixed with air in a ratio 1:6, the ux through the cis membrane (with an H2 content of12.7%) may be detonable, while the ux through the trans membrane (with an H2 content of 10.7%) is not detonable52.

As demonstrated above, each composition in between can be tuned, enabling a remote-controlled adjusting of hazardous or non-hazardous conditions.

In conclusion, we have fabricated a novel MOF membrane, for which permeation, as well as selectivity can be remotely controlled by photoswitching the azobenzene-side-groups decorating the MOF pores. The separation factor of a H2:CO2 mixture was switched between 3 and 8. Moreover, the separation factor, and accordingly the molecular composition of the permeate ux, can be precisely adjusted within this range. This means for this pre-combustion gas mixture, the combustibility and ignition point (when mixed with air) can be continuously tuned by light irradiation of this smart membrane. The concept of switching and continuously tuning the membrane selectivities can be extended to the separation of other gas mixtures, for example, N2:CO2. Further innovative application might be the control of the accessibility to a catalyst or sensor surface and the controlled (selective) release of encapsulated fragrances or drugs. In addition, it could also be profoundly extended to other kinds of membranes like polymeric membranes2 or mixed-matrix MOF membranes9 by functionalizing these materials with photosensitive moieties.

Methods

X-ray diffraction. X-ray diffraction measurements in out-of-plane geometry (also reffered to as co-planar orientation) were carried out using a Bruker D8-Advance diffractometer equipped with a position sensitive detector Lynxeye in yy geometry. Variable divergence slit and 2.3 Soller-slit were used on the secondary side. A Cu-anode with Cu Ka1 radiation (l 0.154 nm) was used. The

measurements were carried out with a scan step of 0.02 at 40 kV and 40 mA.

Infrared reection-absorption spectroscopy. IRRAS of the samples were performed with a resolution of 2 cm 1 using a FTIR spectrometer of type Bruker

VERTEX 80. All the IRRAS results were recorded in grazing incidence reection mode at an angle of incidence of 80 relative to the surface normal using liquid-

nitrogen-cooled mercurycadmiumtelluride mid band detectors. Perdeuterated hexadecanethiol-SAMs on Au/Si were used for reference measurements.

Ultravioletvis spectroscopy. The ultravioletvis spectra were recorded by means of a Cary5000 spectrometer with a UMA unit from Agilent. Ultraviolet irradiation was performed with a 365 nm LED light from PrizMatix with a power or 112 mW. The visible light irradiation was performed with a 455 nm LED light with 135 mW. The distance between the sample and the LED was about 5 cm.

Scanning electron microscopy. SEM cross-section pictures were taken with a eld-emission electron microscope JEOL-JSM-6700 F at 10 kV accelerating voltage and 10 mA emission current. To prevent the sample from charging, carbon was evaporated on the surface to provide a conductive surface coating using a Leica EMSCD500. The working distance was 15 mm.

SAM-preparation. For SAM formation, a clean gold substrate (that is, gold coated siliconwafer) was rinsed with pure ethanol and then immersed in a solution of MUD with a concentration of 1 mM in ethanol for 18 h. Afterwards the substrate was rinsed thoroughly with ethanol and dried under nitrogen stream.

Plasma treatment. The quartz glass and porous aluminium oxide substrates were treated by oxygen plasma (Diener Plasma; 50 sccm, pure O2) for 10 min to remove impurities, as well as increase the number of OH functional groups and the hydrophilicy.

SURMOF synthesis. The experimental procedure used to grow SURMOF lms on functional surfaces has been discussed in detail previously35,37. In summary, the layer-by-layer growth process consists of alternately immersing the substrate in the ethanolic solutions of the building units, that is, the metal knots (here: 1 mM copper acetate) and the organic linkers (here: 0.1 mM AzoBPDC and 0.1 mM AzoBiPyB; the synthesis of the linkers is explained in refs 26,30). Between each immersion step, the substrates were rinsed thoroughly with ethanol. In the present work, the substrates were immersed into copper acetate solution for 15 min, subsequently rinsed with pure ethanol solution for 2 min, and then immersed into the linker solution for 30 min. All solutions were kept at 60 C during MOFlm preparation. The SURMOF lms on porous aluminium oxide supports (asymmetric mesoporous aluminium oxide supports from IKTS Hermsdorf, Germany) were prepared in 90 synthesis cycles. The SURMOF samples for infrared and ultravioletvis spectroscopy were prepared in 60 synthesis cycles on MUD-functionalized gold surfaces and on quartz glass, respectively. Since the sample is protected from light irradiation during the synthesis, all azobenzene-side-groups in the pristine SURMOF lm are in the thermodynamically most stable state, the trans ground state.

Gas permeation. Gas permeation was carried out using an online gas chromatograph Agilent Technologies 7890A. Evaluation of the membrane was performed by mixed-gas permeation. Viton O-Rings (FKM 70 Vi 370) were used to seal the membrane gas-tight in its housing. In-situ irradiation of the membrane layer was achieved by a bre-coupled, monochromatic high power Prizmatix FC-5 LED. Before the permeation data were recorded, the membrane was activated at 50 C in a pure nitrogen ow for 24 h. For pre-combustion hydrogen separation at 25 C, a 50:50 mixture of H2:CO2 was used at ow-rates of 25 ml min 1 each.

The feed-gas was N2 at a 50 ml min 1 ow rate. For post-combustion separation at 35 C, a 90:10 N2:CO2 mixture was used at volumetric ow rates of 45 ml min 1 for N2 and 5 ml min 1 for CO2. There, CH4 was applied on the sweep side at a ow rate of 50 ml min 1. The experiments were performed at ambient pressure, that is, no overpressure was applied.

Data availability. The data sets generated during and/or analysed during the current study are available from the corresponding author on reasonable request.

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Acknowledgements

We gratefully acknowledge funding by the Volkswagen Foundation, by the BIFTM program of the Helmholtz Association and the German Science Foundation (DFG, SFB 1176, SPP 1928 and Ca147/20). Furthermore, we acknowledge support by DFG and Open Access Publishing Fund of Karlsruhe Institute of Technology.

Author contributions

All authors contributed to writing the manuscript and have approved the nal version of the manuscript. Z.W. synthesized the samples and performed the thin lm switching experiments (X-ray diffraction, ultravioletvis, IRRAS). A.K. performed the membrane switching experiments and the SEM measurements. S.G., D.W. and S.B. synthesized the photoswitchable molecules. C.W. and J.C. were involved in planning and supervising the experiments. L.H. planned and supervised the experiments and wrote the manuscript.

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How to cite this article: Wang, Z. et al. Tunable molecular separation by nanoporous membranes. Nat. Commun. 7, 13872 doi: 10.1038/ncomms13872 (2016).

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