8 research outputs found
Synthesis and Characterization of Covalent Triazine Framework CTF-1@Polysulfone Mixed Matrix Membranes and Their Gas Separation Studies
Covalent triazine framework CTF-1 and polysulfone (PSF) are used to form mixed-matrix membranes (MMMs) with 8, 16, and 24 wt% of the porous filler material CTF-1. Studies on permeability and selectivity are carried out concerning the gases O2, N2, CO2, and CH4. CO2 permeability of the synthesized MMMs increases by 5.4 Barrer in comparison to the pure PSF membrane. The selectivity remains unchanged for O2/N2 and CO2/CH4 but was found to be increased for CO2/N2. Further, comparisons to theoretical models for permeability prediction yield a permeability for CTF-1 which is about six times higher than the permeability of PSF. The inverse of the sum of the free fractional volumes (FFV) of the polymer and the filler correlate linearly to the logarithm of the permeabilities of the gases which conversely indicates that the porosity of the filler contributes to the gas transport through the membrane
Mixed-Matrix Membranes of the Air-Stable MOFâ5 Analogue [Co<sub>4</sub>(ÎŒ<sub>4</sub>âO)(Me<sub>2</sub>pzba)<sub>3</sub>] with a Mixed-Functional Pyrazolate-Carboxylate Linker for CO<sub>2</sub>/CH<sub>4</sub> Separation
The synthesis of
the isostructural MOF-5 analogue 3D-[Co<sub>4</sub>(ÎŒ<sub>4</sub>-O)Â(Me<sub>2</sub>pzba)<sub>3</sub>] with
the bi- or mixed-functional pyrazolate-carboxylate linker was improved
by the use of microwave heating instead of previously described conventional
thermal heating, giving a higher yield at drastically shorter reaction
time with nearly doubled BET surface area, smaller size, and less
aggregation. The significantly increased air/moisture stability of
[Co<sub>4</sub>(ÎŒ<sub>4</sub>-O)Â(Me<sub>2</sub>pzba)<sub>3</sub>] compared to MOF-5 made the Co-MOF amenable for the preparation
of moisture-tolerant [Co<sub>4</sub>(ÎŒ<sub>4</sub>-O)Â(Me<sub>2</sub>pzba)<sub>3</sub>]/Matrimid mixed-matrix membranes (MMMs)
without the use of inert conditions. Uniformly embedding of the small
metalâorganic framework (MOF) particles was achieved in the
polymer, without aggregation and with good MOFâpolymer compatibility.
[Co<sub>4</sub>(ÎŒ<sub>4</sub>-O)Â(Me<sub>2</sub>pzba)<sub>3</sub>]/Matrimid MMMs exhibited an improved CO<sub>2</sub>/CH<sub>4</sub> separation performance over neat Matrimid membranes with
an increase in mixed-gas selectivity from 41 for Matrimid to 60 for
the 24 wt % MMM at 3 bar transmembrane pressure, which is also higher
than reported for moisture-sensitive MOF-5/Matrimid MMMs (maximal <i>S</i> = 45)
Comparative Evaluation of Different MOF and NonâMOF Porous Materials for SO2Â Adsorption and Separation Showing the Importance of Small Pore Diameters for LowâPressure Uptake
The search for adsorbents for flue gas desulfurization processes is a current interest. For the first time, a comparative experimental study of SO2 adsorption by porous materials including the prototypical metalâorganic frameworks NH2âMILâ101(Cr), Basolite F300 (Feâ1,3,5âBTC), HKUSTâ1 (CuâBTC), the zeolitic imidazolate frameworks (ZIF)â8, ZIFâ67, the alumosilicate Zeolite Y, the silicoaluminumphosphate (SAPO)â34, Silica gel 60, the covalent triazine framework (CTF)â1, and the active carbon Ketjenblack is carried out. Microporous materials with pore sizes in the range of 4â8Â Ă
or with nitrogen heterocycles are found to be optimal for SO2 uptake in the lowâpressure range. The SO2 uptake capacity at 1 bar correlates with the BrunauerâEmmettâTellerâsurface area and pore volume rather independently of the surface microstructure. Zeolite Y and SAPOâ34 are stable toward humid SO2. The materials Zeolite Y and CTFâ1(600) show the most promising SO2/CO2 selectivity results with an ideal adsorbed solution theory selectivity in the range of 265â149 and 63â43 with a mole fraction of 0.01â0.5 SO2, respectively, at 293Â K and 1 bar.Microporous materials with pore sizes in the range of â4â8Â Ă
and with nitrogen heterocycles are optimal for the uptake of SO2 in the â° range
Encapsulation of a Porous Organic Cage into the Pores of a MetalâOrganic Framework for Enhanced COâ Separation
We present a facile approach to encapsulate functional porous organic cages (POCs) into a robust MOF by an incipient-wetness impregnation method. Porous cucurbit[6]uril (CB6) cages with high COâ affinity were successfully encapsulated into the nanospace of Cr-based MIL-101 while retaining the crystal framework, morphology, and high stability of MIL-101. The encapsulated CB6 amount is controllable. Importantly, as the CB6 molecule with intrinsic micropores is smaller than the inner mesopores of MIL-101, more affinity sites for COâ are created in the resulting CB6@MIL-101 composites, leading to enhanced COâ uptake capacity and COâ/Nâ, COâ/CHâ separation performance at low pressures. This POC@MOF encapsulation strategy provides a facile route to introduce functional POCs into stable MOFs for various potential applications
High performance MIL-101(Cr)@6FDA-mPD and MOF-199@6FDA-mPD mixed-matrix membranes for CO2/CH4 separation
Combination of the polyimide 6FDA-mPD (6FDA = 4,4âČ-hexafluoroisopropylidene diphthalic anhydride and mPD = m-phenylenediamine) and crystallites of the metalâorganic frameworks (MOFs) MIL-101(Cr) or MOF-199 (HKUST-1, Cu-BTC) produces mixed-matrix membranes (MMMs) with excellent dispersion and compatibility of the MOF particles within the polymer matrix. Permeation tests of a binary CO2/CH4 (50/50) gas mixture showed a remarkable increase of CO2 permeabilities for MIL-101(Cr)@6FDA-mPD and significantly higher selectivities for MOF-199@6FDA-mPD. The CO2 permeability increased from 10 (neat polymer) to 50 Barrer for the 24 wt% MIL-101(Cr)@6FDA-mPD membrane (with essentially constant selectivity) due to the high pore volume of MIL-101(Cr). The CO2/CH4 selectivity increased from 54 to 89 from the neat 6FDA-mPD polymer to the 24 wt% MOF-199@6FDA-mPD membrane, apparently due to the high CO2 adsorption capacity of MOF-199.Financial support (MAT2013-40556-R) from the Ministry of Economy and Competitiveness (MINECO) is gratefully acknowledged by JC. The work of CJ was supported by the Federal German Ministry of Education and Research (BMBF) under grant Optimat 03SF0492C.Peer reviewe
Covalent Triazine Frameworks Based on the First Pseudo-Octahedral Hexanitrile Monomer via Nitrile Trimerization: Synthesis, Porosity, and CO2 Gas Sorption Properties
Herein, we report the first synthesis of covalent triazine-based frameworks (CTFs) based on a hexanitrile monomer, namely the novel pseudo-octahedral hexanitrile 1,4-bis(tris(4âČ-cyano-phenyl)methyl)benzene 1 using both ionothermal reaction conditions with ZnCl2 at 400 °C and the milder reaction conditions with the strong BrĂžnsted acid trifluoromethanesulfonic acid (TFMS) at room temperature. Additionally, the hexanitrile was combined with different di-, tri-, and tetranitriles as a second linker based on recent work of mixed-linker CTFs, which showed enhanced carbon dioxide captures. The obtained framework structures were characterized via infrared (IR) spectroscopy, elemental analysis, scanning electron microscopy (SEM), and gas sorption measurements. Nitrogen adsorption measurements were performed at 77 K to determine the Brunauer-Emmett-Teller (BET) surface areas range from 493 m2/g to 1728 m2/g (p/p0 = 0.01â0.05). As expected, the framework CTF-hex6 synthesized from 1 with ZnCl2 possesses the highest surface area for nitrogen adsorption. On the other hand, the mixed framework structure CTF-hex4 formed from the hexanitrile 1 and 1,3,5 tricyanobenzene (4) shows the highest uptake of carbon dioxide and methane of 76.4 cm3/g and 26.6 cm3/g, respectively, at 273 K