Manjuab,
Prasun Kumar Roy*a,
Arunachalam Ramanan*b and
Chitra Rajagopala
aCentre for Fire, Explosive and Environment Safety, DRDO, Delhi-54, India. E-mail: pk_roy2000@yahoo.com
bDepartment of Chemistry, Indian Institute of Technology Delhi, New Delhi-16, India. E-mail: aramanan@chemistry.iitd.ac.in
First published on 1st April 2014
Core–shell poly(dimethylsiloxane) (PDMS)–MOF 5 microspheres were prepared by directed crystallization of MOF 5 on thermally stable PDMS beads. The microspheres were evaluated for their potential use as a stationary phase for gas-chromatographic separation of permanent gases and liquids, where the issues associated with pressure drop were circumvented. The successful demonstration of this simple and versatile methodology widens the scope for large-scale application of Metal–Organic Frameworks (MOFs) in chromatographic separation.
Efficient chromatographic separation in packed columns require the particle size of stationary phase to be large enough to circumvent issues associated with pressure drops (see ESI†). The pressure drop in a packed column is inversely proportional to the particle size, and it becomes increasingly impractical to drive the carrier gas in columns containing smaller particles. Early studies on MOF based chromatographic separations on packed beds relied on large crystals6–8 or MOF pellets9 in relatively short column (2–5 cm). To evade the pressure drop issue, researchers have lately directed their attention towards MOF coated capillary columns which additionally result in efficient separations.4,10,11 However, these columns are rather fragile, and suffer from their inherent problems, arising from uncontrolled film formation on the inner capillary walls. Also, capillary columns require relatively specialized injectors and ancillary flow and pressure controllers. Unfortunately, large scale synthesis of MOFs can only afford polycrystalline materials, which cannot be directly packed in chromatographic columns for reasons mentioned above. To envisage economically viable chromatographic applications of functional MOFs at an industrial level, it is desirable to develop methodologies or processes for integrating smaller crystallites that are amenable for scale-up.
We hypothesise that efficient MOF based separations can very well be performed on conventional packed beds by immobilizing the MOFs on an inert template so as to increase the particle size suitably for use in chromatographic columns. The core material has been selected from the broad group of siloxanes, in view of their excellent thermal stability and their widespread use as a template in the field of soft lithography,12 and MOF 5 was selected based on its celebrated nature. The crystal structure of Zn4(O)(BDC)3 or MOF 5 framework is made of oxocentered Zn4O connected through linear benzenedicarboxylate (BDC) units forming an extended 3D cubic network with interconnected pores of 8 Å aperture width and 12 Å pore diameter (Fig. 1). Inset shows oxo-centered Zn4O tetrahedra connected through linear BDC linkers creating open pores.
Fig. 1 Secondary building unit and crystal structure of MOF 5 (Zn: blue; C: grey; H: white and O: red). |
In this paper, we report a simple procedure for directed crystallisation of MOF 5 on the PDMS microspheres, which have been subsequently employed as a stationary phase for gas chromatographic separations. This route yields particles with core–shell morphology requiring substantially lesser amount of MOFs, which is expected to result in lesser band broadening in the chromatograms compared to fully porous materials, thereby delivering higher efficiencies. The methodology can be applied to prepare any PDMS (core)–MOF (shell) combination, and can be used to generate novel stationary phase for chromatographic separations.
Fig. 2 Surface morphology and elemental analysis of (a) PDMS and (b) core–shell PDMS–MOF 5 microspheres. Inset shows the magnified image of MOF 5 crystallites on the surface. |
The BET surface area was determined by physisorption of N2 at 77 K. The adsorption–desorption isotherms of the MOF 5 loaded microspheres and the core PDMS are presented in Fig. 3. PDMS microspheres exhibited non-porous nature as evidenced by negligible nitrogen uptake and low surface area (8 m2 g−1). The loading of MOF 5 on the core PDMS resulted in a tremendous increase in the surface area (2850 m2 g−1) and the corresponding adsorption isotherms revealed its characteristic microporous nature. To evaluate the adherence of the MOF 5 coating onto the core PDMS, the MOF 5 loaded microspheres were soaked in DMF for 30 min, followed by exposure to ultrasonic water bath (operating frequency 33 kHz) for 15 min. The coating adhered strongly, with the extent of mass loss being negligible (<2%), as estimated gravimetrically.
Fig. 3 N2 adsorption (open symbol) and desorption isotherms (filled symbol) for PDMS–MOF 5. Inset shows the adsorption–desorption isotherms of core PDMS. |
The PXRD pattern of the siloxane core and PDMS–MOF 5 is presented in Fig. 4, which clearly reveals the amorphous nature of PDMS. On the other hand, the XRD of MOF 5 loaded PDMS exhibit distinct diffraction peaks, and the peak positions match with the powder pattern generated by Crystallographic Information File (CCDC-277428).
The TGA traces of the siloxane core, MOF 5 and core–shell microspheres (PDMS–MOF 5) are presented in Fig. 5, which reveal that prepared microspheres exhibit excellent thermal stability and can be used in service till 250 °C.
The FTIR of the PDMS, both before and after MOF loading is presented in Fig. 6. In the FTIR spectra of PDMS, characteristic absorption at 802 and 1258 cm−1 were observed which could be attributed to the (CH3)2SiO group vibration in the polymer. Additionally a broad absorption at 1000–1130 cm−1 was also observed, which can be attributed to the Si–O–Si vibration. Due to the coordination of the carboxylic acid groups with the metal ions, there is a significant shift in the position of the CO absorption band, from 1676 cm−1, in TPA, to 1657 cm−1 in MOF 5 (Fig. 6b). Coordination of the linker with the metal ions leads to the disappearance of the CO absorption band at 1281 cm−1 and the broad absorption due to the hydroxyl groups ∼3000–3200 cm−1.
Fig. 7 Gas chromatograms showing effective separations of H2, N2, CO, CH4 and CO2. Inset shows the gas chromatogram exhibiting excellent separation of liquids. |
The retention time of each component, as determined by injection of individual gas separately, is given in the ESI (see Table S1, ESI†). The order of elution of the individual gases from the column is in accordance with increasing order of their kinetic diameters (H2, 2.89 Å; N2, 3.64 Å; CO, 3.76 Å; CH4, 3.8 Å and CO2, 3.3 Å). It is to be noted that the estimated pore size of MOF 5 is too large (∼9 Å) to permit separations based on molecular sieving, and hence the sequence of elution is very well expected. Interestingly, CO2 with a kinetic diameter of 3.3 Å elutes at the end, which can be explained on the basis of strong interaction of CO2 with the MOF 5 framework.16 The efficiency of the packed PDMS–MOF 5 column towards separation of liquids was also established by injecting an equimolar mixture of methanol, propanol and acetone which were detected using flame ionisation technique. The chromatogram (response of FID) as shown in the inset of Fig. 7, clearly establishes the ability of the column towards separation of liquid mixtures. Since the kinetic diameter of all the molecules is lesser than the pore size of MOF-5, the order of elution is in line.
For comparison purpose, chromatographic separations were also performed on commercially available packed columns generally employed for separation of similar gas mixtures, namely molecular sieve 5A (MS 5) and Porapak N. The chromatograms obtained are shown in the ESI.† Carbon dioxide does not elute from MS 5 column due to its strong interactions with the microporous aluminosilicate structure, while Porapak N is incapable of separating H2 and N2 mixture.17 It can be seen that neither of these columns individually could separate all the components, however a 2D separation can be used for effective separations.
The prepared column was also employed to separate a natural gas mixture comprising of 79.37% methane, 6.72% ethane, 0.94% iso-butane, 0.53% iso-pentane, 1.31% N-butane, 0.19% N-hexane, 0.51% N-pentane, 8.09% propane and 2.34% CO2 (% v/v). For this purpose, 50 μL of the gas mixture was injected into the GC column and the separation was effected under conditions mentioned in the ESI.† The TCD response is presented in Fig. 8. The retention time of each component, as determined by injection of individual gas separately, is given in the ESI (see Table S2, ESI†). It can be seen that all the components could be effectively separated by the PDMS–MOF 5 column.
Fig. 8 Gas chromatogram showing separation of natural gas mixture. (1) Methane, (2) ethane, (3) propane, (4) carbon dioxide, (5) iso-butane, (6) n-butane, (7) n-pentane, (8) n-hexane. |
Our study clearly highlights the potential of MOF loaded microspheres for practical application towards separation of gas mixtures. The reproducibility of the PDMS–MOF 5 column was established by performing repeated runs on gas mixtures obtained from ethanol reforming exit stream,18 comprising primarily of H2, N2, CH4, CO2 and CO, which corroborates excellent separation reproducibility.
It should be noted that in view of tunability of the pore size of MOFs by judicious choice of SBU and linker molecules, it is possible to envisage hitherto unprecedented separations, thereby opening novel opportunities in the field of separation technology.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c4ra00894d |
This journal is © The Royal Society of Chemistry 2014 |