Composite Metal Organic Framework Materials, Processes for Their Manufacture and Uses Thereof
20200179916 ยท 2020-06-11
Inventors
- David Fairen-Jimenez (Cambridge, GB)
- Tian Tian (Cambridge, GB)
- Joshua Mehta (Cambridge, GB)
- Andrew Wheatley (Cambridge, GB)
- Bethany Connolly (Cambridge, GB)
Cpc classification
B01J20/28019
PERFORMING OPERATIONS; TRANSPORTING
B01J20/3078
PERFORMING OPERATIONS; TRANSPORTING
B01J20/3204
PERFORMING OPERATIONS; TRANSPORTING
B01J20/3293
PERFORMING OPERATIONS; TRANSPORTING
Y02W10/37
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B01J35/30
PERFORMING OPERATIONS; TRANSPORTING
B01J35/40
PERFORMING OPERATIONS; TRANSPORTING
B01J20/226
PERFORMING OPERATIONS; TRANSPORTING
B01J20/06
PERFORMING OPERATIONS; TRANSPORTING
B01J21/063
PERFORMING OPERATIONS; TRANSPORTING
B01J37/0009
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
B01J21/06
PERFORMING OPERATIONS; TRANSPORTING
B01J37/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A monolithic metal-organic framework (MOF) composite body is disclosed, comprising: MOF crystallites adhered to each other via a binder comprising MOF; and at least 0.15 vol % nanoparticles encapsulated in the MOF body. The nanoparticles have an average particle size corresponding to an average particle diameter in the range 3-200 nm. The nanoparticles may have photocatalytic activity. The MOF composite body is of use for treating water containing an organic dye, the photocatalytic reaction supported by the photocatalytic nanoparticles being a degradation reaction of the organic dye.
Claims
1. A monolithic metal-organic framework (MOF) composite body selected from the group consisting of: (i) a MOF composite body comprising: MOF crystallites adhered to each other via a binder comprising MOF; at least 0.15 vol % nanoparticles encapsulated in the MOF body, the nanoparticles having an average particle size corresponding to an average particle diameter in the range 3-200 nm; and (ii) a MOF composite body consisting of: MOF crystallites; a binder formed of MOF which binds the MOF crystallites together in the body; at least 0.15 vol % nanoparticles encapsulated in the MOF body, the nanoparticles having an average particle size corresponding to an average particle diameter in the range 3-200 nm; optionally, residual solvent; and optionally, one or more additives, wherein the additives are present in an amount of not more than 10% by mass of the composite body.
2. (canceled)
3. The monolithic MOF composite body according to claim 1 wherein the nanoparticles are photocatalytic nanoparticles.
4. The monolithic MOF composite body according to claim 1 wherein the relative photonic efficiency .sub.r of the nanoparticles is greater than 1.
5. The monolithic MOF composite body according to claim 1 wherein the nanoparticles are present in the composite in an amount of at most 1 vol %, based on the volume of the composite.
6. The monolithic MOF composite body according to claim 1 wherein the nanoparticles comprise a composition selected from the group consisting of one or a combination of: metal oxides, including for example SnO.sub.2, ZnO, TiO.sub.2, PdO; Pd, Au, Ru, Rh, Pt; Bi-containing compositions, including for example BiFeO.sub.3, Bi.sub.2S.sub.3, BiVO.sub.4 and Bi.sub.2Fe.sub.3O.sub.9; Cd-containing materials, including for example CdSe and CdS; transition metal dichalcogenides, including for example MoS.sub.2 and WS.sub.2.
7. The monolithic MOF composite body according to claim 6 wherein the nanoparticles comprise at least two different materials having a heterojunction interface between them.
8. The monolithic MOF composite body according to claim 1 wherein the smallest dimension of the composite body is at least 2 mm.
9. The monolithic MOF composite body according to claim 1 having a BET surface area of at least 500 m.sup.2g.sup.1.
10. The monolithic MOF composite body according to claim 9 wherein the nanoparticles, when isolated from the MOF composite body have a BET surface area of at most 100 m.sup.2 g.sup.1.
11. The monolithic MOF composite body according to claim 1 wherein the MOF comprises a zeolitic imidazolate framework (ZIF).
12. The monolithic MOF composite body according to claim 1 wherein the MOF comprises one or more materials selected from the group consisting of: ZIF-8, HKUST-1, UiO-66, MOF-74, Al-fumarate, NU-1000, MIL-100, MIL-53.
13. (canceled)
14. A process for manufacturing a monolithic metal-organic framework (MOF) composite body, the process comprising the steps: providing MOF precursors; providing nanoparticles having an average particle size corresponding to an average particle diameter in the range 3-200 nm; providing at least one solvent; allowing the reaction of the MOF precursors in the solvent in the presence of the nanoparticles; carrying out a drying stage with a maximum temperature in the drying stage of not more than 80 C. to form a monolithic MOF composite body comprising MOF crystallites adhered to each other via a binder comprising MOF, and incorporating at least 0.15 vol % of the nanoparticles encapsulated in MOF.
15. The process according to claim 14 wherein the drying stage is carried out in a mould so that the composite body is formed to conform to an internal shape of the mould.
16. A method for treating fluid, the method comprising: providing a MOF composite body selected from the group consisting of: (i) a MOF composite body comprising: MOF crystallites adhered to each other via a binder comprising MOF; at least 0.15 vol % nanoparticles encapsulated in the MOF body, the nanoparticles having an average particle size corresponding to an average particle diameter in the range 3-200 nm; and (ii) a MOF composite body consisting of: MOF crystallites; a binder formed of MOF which binds the MOF crystallites together in the body; at least 0.15 vol % nanoparticles encapsulated in the MOF body, the nanoparticles having an average particle size corresponding to an average particle diameter in the range 3-200 nm; optionally, residual solvent; and optionally, one or more additives, wherein the additives are present in an amount of not more than 10% by mass of the composite body; and contacting the MOF composite body with a fluid to be treated, the nanoparticles interacting with the fluid to be treated.
17. The method according to claim 27 wherein the water to be treated contains an organic dye, the photocatalytic reaction supported by the photocatalytic nanoparticles being a degradation reaction of the organic dye.
18. The method according to claim 17 wherein the organic dye is one or a combination of organic dyes selected from the group consisting of: eosin dyes, rhodamine dyes, xanthene dyes, fluorescein dyes, acridine dyes, anthraquinone dyes, azo dyes, diazonium dyes, fluorine dyes, fluorone dyes, phthalocyanine dyes.
19. The method according to claim 27 wherein the nanoparticles comprise a composition selected from the group consisting of one or a combination of: metal oxides, including SnO2, ZnO, TiO2, Bi-containing compositions, including BiFeO3, Bi2S3, BiVO4 and Bi2Fe3O9 Cd-containing materials, including CdSe and CdS transition metal dichalcogenides, including MoS2 and WS2.
20. The method according to claim 27 wherein the electromagnetic radiation is natural sunlight or artificial sunlight.
21. (canceled)
22. The method according to claim 16 wherein the fluid to be treated comprises CO and the nanoparticles comprise Au, the CO being treated by being oxidised.
23. The method according to claim 16 wherein the fluid to be treated comprises hydrogen and the nanoparticles comprising one or more of: Ru, Ru/Rh, Pt, Pd resulting in a hydrogenation reaction.
24. The method according to claim 16 wherein the fluid to be treated comprises water and the nanoparticles comprise Ru, resulting in a hydration reaction.
25. The method according to claim 16 wherein the fluid to be treated comprises methane and the nanoparticles comprising one or more of: PdO/Au/TiO.sub.2 or Au @ PdO/TiO.sub.2 resulting in a methane oxidation reaction to form methanol.
26. The method according to claim 16 wherein the fluid to be treated comprises water and the nanoparticles comprise Pt, resulting in the formation of hydrogen and oxygen.
27. The method for treating fluid according to claim 16, wherein the fluid is water, the nanoparticles being photocatalytic nanoparticles, the method comprising allowing the MOF composite bodies in contact with the water to be treated to be subjected to electromagnetic radiation suitable for activating at least one photocatalytic reaction supported by the photocatalytic nanoparticles.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0077] Embodiments of the invention will now be described by way of example with reference to the accompanying drawings in which:
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for SnO.sub.2 nanoparticles prepared using a hydrothermal method.
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[0093] .sub.monoZIF-8 (large filled diamonds)
[0094] SnO.sub.2@.sub.monoZIF-8 (filled squares)
[0095] SnO.sub.2@.sub.monoZIF-8 after 1 catalytic cycle (small filled diamonds)
[0096] SnO.sub.2@.sub.monoZIF-8 after 5 catalytic cycles (filled triangles)
[0097] SnO.sub.2@.sub.monoZIF-8 after 10 catalytic cycles (filled circles)
[0098] SnO.sub.2@.sub.monoZIF-8 after 1 water cycle (open diamonds)
[0099] SnO.sub.2@.sub.monoZIF-8 after 5 water cycles (open triangles)
[0100] SnO.sub.2@.sub.monoZIF-8 after 10 water cycles (open circles)
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DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS, AND FURTHER OPTIONAL FEATURES OF THE INVENTION
[0123] The photocatalytic degradation of toxic dye effluents has received considerable attention. Despite semiconducting nanoparticles being promising photocatalysts for the degradation of these compounds, their powder morphology has previously hindered applications due to poor catalyst retention and recyclability. Furthermore, applications development faces difficulties owing to particle toxicity and agglomeration. We disclose here, in one embodiment of the invention, a new type of composite material involving the in situ immobilization of tin oxide nanoparticles (SnO.sub.2NPs) within a monolithic metal-organic framework (MOF), the zeolitic imidazolate framework ZIF-8. SnO.sub.2@.sub.monoZIF-8 exploits the mechanical properties and structural resilience of a monolithic MOF, whilst leveraging the catalytic action of the nanoparticles. The composite displays outstanding photocatalytic properties with full retention of activity observed after 10 catalytic cycles and represents a substantial advance in the field of treating toxic effluents and a vital validation for commercial application.
[0124] Zeolitic imidazolate frameworks (ZIFs) are MOFs with zeolitic topologies based on large cages and narrow windows [Ref. 1]. ZIF-8 (Zn(2-mlm).sub.2, 2-mlm=C.sub.4H.sub.5N.sub.2.sup.) in particular, boasts both high porosity (1.16 nm cavity diameter; flexible 0.34 nm window diameter [Ref. 2]; total pore volume 0.485 cm.sup.3 g.sup.1) and high chemical and thermal stability [Ref. 3]. However, despite their industrial potential, MOFs and ZIFs are almost invariably synthesized in powdered or thin film morphologies [Ref. 4]. In a recent major advance in MOF shaping, we presented a novel sol-gel synthetic method for producing transparent, robust, monolithic ZIF-8 without the need for high pressures or binders [Ref. 5]. These monoliths retained the same porous texture and chemical stability of the powder [Ref. 6] but now in the form of a mechanically robust macrostructure with bulk densities and volumetric BET areas 3-4 times higher than those of the powder. Compared with other pelletization methods that can lead to up to 90% of pore collapse due to the use of high pressures [Ref. 7], this synthetic protocol and monolithic morphology introduces the possibility of creating mechanically stable supports based on porous MOFs that can incorporate highly active and potentially toxic species such as nanoparticles (NPs) [Refs. 8 and 9].
[0125] The incorporation of catalytically active NPs, in one embodiment, into a MOF represents a method of exploiting the combined physico-chemical properties of both constituents [Ref. 10]. However, to the best of the inventors' knowledge, there are no reports of nanoparticle encapsulation via a bottom up synthesis involving MOF precursors resulting in a mechanically stable monolithic composite (NP@.sub.monoMOF) recoverable by simple filtration. Previous attempts to exploit the properties of MOFs for environmental remediation have focused on powdered morphologies, with their ability to degrade toxic organic compounds being poor [Ref. 11]. In this work, we synthesize mechanically and chemically robust monolithic SnO.sub.2@.sub.monoZIF-8, in one embodiment. This composite combines excellent activity in the degradation of toxic industry effluent with straightforward catalyst recyclability.
[0126] We chose SnO.sub.2NPs for encapsulation due to their non-toxic nature and track record in detoxification [Refs. 12, 13]. This photocatalyst, however, is considered to present major problems of recovery and reuse owing to the small size of the NPs [Ref. 14]. The synthesis of SnO.sub.2NPs resulted in uniform, monocrystalline NPs with a mean size distribution of ca. 5.01.1 nm (
[0127] We confirmed the composition of SnO.sub.2@.sub.monoZIF-8 using energy-dispersive X-ray spectroscopy (EDX).
[0128] X-ray photoelectron spectroscopy (XPS) confirmed the results of FIB-SEM.
[0129]
TABLE-US-00001 TABLE 1 BET areas (S.sub.BET), micropore volumes (W.sub.0), and total pore volumes (V.sub.TOT) for .sub.monoZIF-8 and SnO.sub.2@.sub.monoZIF- 8 before and after exposure to MB and H.sub.2O. S.sub.BET W.sub.0.sup.[a| V.sub.TOT.sup.[b] Material [m.sup.2g.sup.1] [cm.sup.3 g.sup.1] [cm.sup.3 g.sup.1] .sub.monoZIF-8 1423 0.543 0.546 SnO.sub.2@.sub.monoZIF-8 1055 0.413 0.417 SnO.sub.2@.sub.monoZIF-8 - 1 cycle (MB) 1068 0.421 0.427 SnO.sub.2@.sub.monoZIF-8 - 5 cycle (MB) 985 0.389 0.393 SnO.sub.2@.sub.monoZIF-8 - 10 cycle (MB) 1027 0.405 0.411 SnO.sub.2@.sub.monoZIF-8 - 1 cycle (H.sub.2O) 973 0.384 0.389 SnO.sub.2@.sub.monoZIF-8 - 5 cycle (H.sub.2O) 991 0.389 0.393 SnO.sub.2@.sub.monoZIF-8 - 10 cycle (H.sub.2O) 996 0.395 0.399 .sup.[a]Data obtained at P/P.sub.0 = 0.1 .sup.[b]P/P.sub.0 = 0.99.
[0130] We assessed the photocatalytic activity of SnO.sub.2@.sub.monoZIF-8 using aqueous methylene blue (MB) over multiple catalytic cycles. Each cycle lasted 3 hours, with the composite recovered each time by simple gravity filtration (
[0131] Interestingly, although the narrow apertures of ZIF-8 preclude the passage of MB, this is not a barrier to photocatalysis. Houas et al. have proposed the following mechanism [Ref. 19], where intimate contact between SnO.sub.2NPs and dye is not necessary:
TABLE-US-00002 SnO.sub.2 + hv .fwdarw. e.sup..sub.CB + h.sup.+.sub.VB 1) Exciton production O.sub.2 + e.sup..sub.CB .fwdarw. O.sub.2.sup. 2) Ionosorption and reduction of O.sub.2 (0 to 0.5 eV) H.sub.2O + h.sup.+.sub.VB .fwdarw. H.sup.+ + OH.sup. 3) Production of hydroxyl radicals O.sub.2.sup. + H.sup.+ .fwdarw. HO.sub.2.sup. 4) Neutralisation of O.sub.2.sup. 2HO.sub.2.sup. .fwdarw. H.sub.2O.sub.2 + O.sub.2 5) H.sub.2O.sub.2 formation H.sub.2O.sub.2 + e.sup..sub.CB .fwdarw. OH.sup. + OH.sup. 6) H.sub.2O.sub.2 degradation R + OH.sup. .fwdarw. R.sup. + H.sub.2O 7) Oxidation of dye (R)
[0132] In this mechanism, the species active in dye degradation derive from adsorbed oxygen and water [Ref. 14]. In our case, we propose that water, with a 2.68 kinetic diameter [Ref. 21], diffuses through the ZIF-8 windows [Ref. 22] and interacts with SnO.sub.2. Reaction with the photoinduced excitons (electrons, e.sup., and holes, h.sup.+) in the conduction (CB) and valence (VB) bands of the NPs then creates the hydroxyl and superoxide radicals required for dye degradation. The high levels of photocatalytic activity achieved using SnO.sub.2@.sub.monoZIF-8 suggest that SnO.sub.2 far below the monolith surface, and not only that present at the external surface, must be intrinsically involved in the catalytic cycle.
[0133] We evaluated the chemical robustness of SnO.sub.2@.sub.monoZIF-8 by PXRD and N.sub.2 adsorption. PXRD patterns of the composite after 1, 5 and 10 photocatalytic cycles showed no significant variations from that of fresh composite (
[0134] Industrial applications require that materials possess the mechanical strength and toughness to withstand the stresses of friction, cyclic compression or vibration within a container. We used the nanoindentation technique to establish that the magnitudes of both the Young's modulus, E, and Hardness, H, of SnO.sub.2@.sub.monoZIF-8 (3.300.01 GPa and 0.440.01 GPa, respectively) were about 10% greater than those of .sub.monoZIF-8 (3.000.01 GPa and 0.410.01 GPa, respectively), thereby rendering the composite structurally stiffer and more resistant to permanent deformation (
[0135] In summary, we report a chemically and mechanically robust composite in which SnO.sub.2NPs have been controllably integrated into a monolithic metal-organic framework without the need for binders, additives or high pressures, so avoiding structural amorphization and pore collapse. SnO.sub.2@.sub.monoZIF-8 has shown high levels of photocatalytic activity and extraordinary recyclability when compared to powdered nanoparticles or previously reported NP@MOF composites. Furthermore, the straightforward synthetic method used led to the immobilization of nanoparticles in a way that prevented high degrees of agglomeration. The outstanding level of recyclability coupled with the unprecedented degree of dye degradation seen under high loading of the composite has proven SnO.sub.2@.sub.monoZIF-8 to be a highly effective photocatalyst.
[0136] Synthesis of SnO.sub.2 Nanoparticles
[0137] SnO.sub.2NPs were prepared following a modified literature synthesis [Ref. 24]. SnCl.sub.4.5H.sub.2O (0.787 g, 2.24 mmol) was dissolved in water (15 mL). Sodium hydroxide (0.7 g, 17.5 mmol) was dissolved in water (20 mL) and ethanol (20 mL). This was added dropwise to the stannic chloride solution until a pH of 12 was achieved. The mixture was transferred quantitatively (ca. 40 mL) to an autoclave and hydrothermally treated (200 C., 24 hours). After cooling, the resultant precipitate was separated and washed with water and 1:1 ethanol/water mix under centrifugation (7000 rcf). The washed sample was dried in a desiccator overnight, yielding SnO.sub.2NPs as a white powder.
[0138] Synthesis of SnO.sub.2@.sub.monoZIF-8 Monoliths
[0139] Zn(NO.sub.3).sub.2.6H.sub.2O (0.293 g, 0.985 mmol) was dissolved in ethanol (20 mL). 2-methylimidazole (C.sub.4H.sub.6N.sub.2) (0.809 g, 9.85 mmol) was dissolved separately in ethanol (20 mL), and SnO.sub.2NPs were added (30 mg, 0.198 mmol). Both solutions were ultrasonicated for 20 minutes before being combined. The resulting mixture was stirred for 15 minutes at room temperature then centrifuged (4250 rcf, 10 minutes). The collected solid was washed in ethanol (20 mL, 3 times) and the pellet dried at room temperature overnight, yielding a solid monolith. This was ground into 1-5 mm pieces before activation at 110 C. in a vacuum oven overnight.
[0140] Characterization of Materials
[0141] Zn(NO.sub.3).sub.2.6H.sub.2O (98%) and 2-methylimidazole (97%) were purchased from Alfa Aesar; ethanol (>99.5%), SnCl.sub.4.5H.sub.2O and methylene blue were purchased from Sigma-Aldrich; NaOH pellets (>97%) were purchased from Fischer Scientific. Chemicals were used as received, without further purification. SnO.sub.2@.sub.monoZIF-8 was characterised utilising: focused ion beam-X-ray photoelectron spectroscopy (FIB-XPS), focused ion beam-scanning electron microscopy (FIB-SEM), transmission electron microscopy (TEM), scanning transmission electron microscopy-energy dispersive X-ray spectroscopy (STEM-EDX), thermogravimetric analysis (TGA), powder X-ray diffraction (PXRD), N.sub.2 adsorption isotherms at 77 K, mercury porosimetry, nanoindentation studies, attenuated total reflectance FT infrared spectroscopy (FT-IR), inductively coupled plasma-optical emission spectroscopy (ICP-OES) and elemental analysis (EA) techniques.
[0142] Photocatalytic properties were explored by monitoring the degradation of model organic volatile methylene blue (MB) under simulated solar irradiation produced by a 150 W xenon lamp fitted with an air mass 1.5 global (AM 1.5 G) filter (Solar Simulator model LSO106, 1 sun illumination, 100 mW cm.sup.2). The degradation of aqueous MB (25 mL, 1.5510.sup.5 M, pH 7.30) was recorded by monitoring the reduction in .sub.max at 664 nm using a BOECO S-22 and a Perkin Elmer Lambda 750 UV/vis/NIR spectrometer for single and multi-wavelength measurements, respectively. An ice-cold water bath prevented dye evaporation under impeding light and thermal dye degradation. Control experiments were run (i) without irradiation in the presence of SnO.sub.2@.sub.monoZIF-8 and (ii) with irradiation in the absence of composite. Low loading experiments used 0.4 g of composite, whilst high loading sets used 1.7 g. Composite was collected under gravity filtration and dried under ambient conditions overnight before recycling. Each cycle under solar irradiation was performed parallel to a control in the dark, administering the same recycling procedure. All experiments were triplicated. Hydroxyl radicals produced during photocatalysis were detected using a terephthalic acid probe.
[0143] PXRD patterns were measured on a PANalytical Empyrean diffractometer fitted with an X'celerator detector and using a Cu-K.sub.1 (=1.5406 ) source with a step size of 0.002 and a scanning speed of 0.022 s.sup.1 at 40 kV and 40 mA. SEM images were obtained on a FEI Helios Nanolab with an accelerating voltage of 5 keV. TEM images were collected on a FEI Tecnai G2 and a FEI Osiris S/TEM operated in scanning mode with an accelerating voltage of 200 keV. For the TEM images of the mother liquor, a 1 mL sample of the reaction medium was withdrawn after 15 minutes and diluted 10 times in ethanol. 25 L of the resulting solution was drop-coated onto a copper grid and the ethanol evaporated at room temperature. For high angle annular dark field (HAADF) images and EDX analysis the monolithic sample was pressed into a copper grid, with the EDX signal collected using a set of Bruker Super-X detectors. Thermogravimetric analyses were performed on TA Instruments TGA 500, ranging from room temperature to 750 C. in nitrogen, using a ramp rate of 10 C. min.sup.1. N.sub.2 adsorption isotherms were obtained at 77 K using a Micrometrics 3 Flex instrument. All samples were degassed in situ at 110 C. for 6 hours before measurement. The recycled SnO.sub.2@.sub.monoZIF-8 samples were not washed after photocatalysis. Mercury porosimetry data was obtained using an AutoPore IV 9500 instrument employing pressures up to 2000 bar. An Exeter analytical CE 440 elemental analyser at a combustion temperature of 975 C. was utilised for C, H, and N analysis whilst Zn and Sn analysis was performed on a Thermo Scientific iCAP 7400 ICP-OES analyser against 1 ppm and 10 ppm standards. SnO.sub.2@.sub.monoZIF-8 was filtered, soaked in deionised water, and dried under conventional and vacuum oven environments before elemental analyses were performed again. FIB-XPS measurements were obtained using a Thermo Scientific K-Alpha system. The binding energy was calibrated internally based on the C(1s) line position. Each etch was conducted at full power (ion energy=3000 eV, current=high) for 20 seconds. The estimated sputter rate of the Ta.sub.2O.sub.5 source was 0.68 nm sec.sup.1, leading to an estimated total etching depth of 122 nm, whilst the diameter of the area analysed was 400 m. FT-IR spectra were collected on a Thermo Scientific Nicolet iS50 FT-IR spectrometer in ATR mode. Nanoindentation measurements were performed using an MTS Nano Indenter XP system equipped with a Berkovich diamond tip. The continuous stiffness method was employed and epoxy mounted monolithic samples were indented up to a maximum surface penetration depth of 2000 nm, in accordance with the established methodology for characterizing MOFs [Ref. S1], taking Poisson's ratio of 0.33 [Ref. S2], to determine the upper bounds of Young's modulus, E. In photocatalytic experiments, 3 mL aliquots taken at 15-minute intervals over three hours gave the concentration of dye as a function of time. Each aliquot was returned to the original dye solution immediately after analysis. Hydroxyl radicals (OH.sup.) produced during photocatalysis were detected by dispersing 0.4 g of SnO.sub.2@.sub.monoZIF-8 in a basic aqueous solution of terephthalic acid (10.sup.4 M). The solution was exposed to simulated solar irradiation and the maximum fluorescence emission intensity of 2-hydroxyterephthalic acid measured after excitation at 315 nm.
[0144] The diffraction pattern (
where D is the mean crystallite size, is the full-width-at-half-maximum (FWHM) in radians, is the angle in degrees, is the wavelength of incident radiation (1.5406 for the Cu-K.sub.1 source), is the strain in the crystallite lattice, K is the dimensionless shape factor and k is a constant, typically close to unity [Ref. S3].
[0145] The (110), (211), (112), (202) and (200) peaks were utilized in the Williamson-Hall analysis (Equation S2), assuming a constant of unity.
was plotted against
to give an intercept of
and gradient , which were used to determine crystallite size and lattice strain respectively.
[0146] Peak broadening in the PXRD pattern indicated small particle size, with the Scherrer formula (Equation S1) giving an average crystallite size of 5.03 nm, assuming a dimensionless shape factor of 0.89 (
[0147] SnO.sub.2 @.sub.monoZIF-8 Analysis
TABLE-US-00003 TABLE S1 Chemical microanalyses of .sub.monoZIF-8 (simulated and experimental) and fresh SnO.sub.2@.sub.monoZIF-8 based on nitrogen and tin contributions acquired from elemental analysis and ICP-OES data. Errors were determined using the standard deviation in triplicated Sn and N wt % values with zero readings occurring due to numerical rounding. Deviation from 100% total loading is attributed to residual reagents and solvents trapped in the materials. Composition Wt. % Materials C H N Sn Zn SnO.sub.2 ZIF-8 Sim. ZIF-8 42.2 4.4 24.6 28.7 100 Exp. .sub.monoZIF-8 41.7 0.0 4.5 0.0 24.4 0.3 26.2 0.4 99.0 1.1 SnO.sub.2@.sub.monoZIF-8 40.5 0.4 4.6 0.1 23.1 0.3 1.6 0.1 24.5 0.4 2.0 0.1 93.9 1.2
[0148] The O(1s) etched levels revealed a peak at 530.6 eV, characteristic of lattice oxygen in SnO.sub.2 (
[0149] Inspection of the cavity dimensions of pure ZIF-8 (11.6 ) indicates that the nanoparticles do not reside in the MOF pores, which are too small to accommodate them. Instead, the nanoparticles are encapsulated by the grown ZIF-8 matrix.
[0150] Control experiments for the photocatalytic degradation of MB were performed: (i) without solar irradiation in the presence of composite (SnO.sub.2@.sub.monoZIF-8) and (ii) with solar irradiation in the absence of composite (
[0151] The degree of degradation was calculated according to the reduction in absorption for the major MB absorption band at .sub.max=664 nm over 3 hours:
[0152] where C.sub.0 is the starting concentration of MB and C.sub.t is the concentration of MB after time t.
[0153] Triplicated data indicate an average degradation of 18.31.4% under simulated solar irradiation in the absence of composite. Error is calculated from the standard deviation in triplicated values. A number of MOFs are known to have photocatalytic properties of their own [Refs. S9 and S10], with the partial degradation of MB under nanoparticulate ZIF-8 previously attributed to the wide band gap of the semiconducting material. This was explained by the proposed ligand-to-metal-charge-transfer (LMCT) of a 2p HOMO electron from the nitrogen linker into the empty zinc LUMO orbital under stimulation from a UV source [Refs. S11 and S12]. For these reasons it was essential to establish whether .sub.monoZIF-8 represented a source of potential dye degradation in the current work. Triplicated control experiment (iii) revealed that .sub.monoZIF-8 presents no photocatalytic behavior under simulated solar irradiation, with measured dye degradation attributable to surface physisorption. This is consistent with literature solid-state UV-Vis data for powdered ZIF-8, which suggests that a large band gap of 4.9 eV prevents exciton formation under solar irradiation [Ref. S13]. However, inspection of the valence and conduction band potentials of SnO.sub.2 reveals that they are positioned such that production of hydroxyl and superoxide radicals, the key species responsible for dye degradation [Refs. S14 and S15], is thermodynamically viable [Ref. S16].
[0154] The thermal stability of fresh and recycled SnO.sub.2@.sub.monoZIF-8 was measured by TGA. We found that the decomposition temperature for SnO.sub.2@.sub.monoZIF-8 (450-500 C.) is lower than that of .sub.monoZIF-8 (600 C.). This is expected due to the nanoparticles disrupting the coordination bonds within the MOF, promoting thermal decomposition [Ref. S17].
[0155] Even allowing for their flexibility, the narrowness of the 3.4 windows of ZIF-8 suggests that the dye cannot pass through its framework apertures. Dye adsorption is thought to occur predominantly via physisorption to the external surface of the monoliths rather than via chemisorption or coordination to zinc clusters [Refs. S6 and S18]. Spectra for SnO.sub.2, .sub.monoZIF-8, fresh SnO.sub.2@.sub.monoZIF-8 and SnO.sub.2@.sub.monoZIF-8 after 10 catalytic cycles were recorded in the range of 400-4000 cm.sup.1 (
[0156] A terephthalic acid (TA) probe was used to prove OH.sup. radical production. Reaction of TA with OH.sup. radicals generates the fluorescent species 2-hydroxyterephthalic acid. The formation of this molecule was monitored using the maximum intensity at 450 nm after excitation at 315 nm, and it was seen to increase with irradiation time (
[0157] The vol % of nanoparticles in the composite is determined based on the density of the nanoparticles, the wt % of the nanoparticles and the density of the composite. In the example of SnO.sub.2@.sub.monoZIF-8, the nanoparticles of SnO.sub.2 have density 6.95 g/cm.sup.3 and 2 wt % and the density of the composite is 1.13 g/cm.sup.3.
[0158] Relative Photonic Efficiency .sub.r
[0159] It is known in the art of photogenerated catalysis and catalysed photolysis that it can be important to provide for the reliable determination and comparison of the efficiency of a particular photocatalyst material to catalyse the degradation of a particular target molecule when subjected to a particular excitation radiation. Therefore in this disclosure the relative photonic efficiency .sub.r of the nanoparticles is considered. The relative photonic efficiency .sub.r of the nanoparticles can be represented as:
[0160] wherein:
[0161] R.sup.in(P25) is the initial rate of degradation of 200 M phenol in an air-equilibrated aqueous dispersion by standard titania particles (Degussa P-25 TiO.sub.2) at 2 g/L under AM1 simulated sunlight radiation.
[0162] R.sup.in(nanoparticles) is the initial rate of degradation of 200 M phenol in an air-equilibrated aqueous dispersion by the nanoparticles (isolated from the MOF of the composite body) at 2 g/L under AM1 simulated sunlight radiation.
[0163] Other than the nature of the catalyst particles, the experiments to determine R.sup.in(P25) and R.sup.in(nanoparticles) are carried out in identical experimental conditions. This follows the guidance for the determination of relative photonic efficiency .sub.r given by Serpone and Salarino (1999) [Ref. S28], the entire content of which is hereby incorporated by reference.
[0164] In effect, therefore, r of the nanoparticles is determined relative to the corresponding photocatalytic efficiency of a standard catalyst (P-25 titania) to degrade a standard target molecule (phenol) under otherwise identical experimental conditions.
[0165] Degussa P-25 TiO.sub.2 consists of two crystalline phases, with about 80% anatase and about 20% rutile and contains traces of SiO.sub.2, Al.sub.2O.sub.3, HCl and Fe. It is nonporous with a BET specific surface area of about 55 m.sup.2/g. The particle diameter is in the range 25 to 35 nm.
[0166] R.sup.in(P25) and R.sup.in(nanoparticles) are tested using a method based on Kar et al. (2016) [Ref. S29]. The method is as follows. Composite containing 5.0 mg of catalyst (from ICP analysis) to be added to 25 mL of a 1.010.sup.5 M aqueous solution of dye (pH 7), and the mixture stirred in the dark for 2 hours to allow adsorption on the composite surface. Determine the absorption of a 3.0 mL aliquot of the mixture by UV-Vis to obtain the dye concentration before photocatalysis (C0) then return the aliquot to the reaction. Irradiate with a 150 W xenon lamp fitted with an air mass 1.5 global (AM 1.5 G) filter (1 sun illumination, 100 mW cm.sup.2). 3 mL aliquots to be taken at 15 minute intervals over 3 hrs to obtain the concentration of dye as a function of time by UV-Vis. Each aliquot to be returned to the original dye solution immediately after analysis. Use an ice cold water bath to prevent evaporation during catalysis and to avoid degradation due to heating. Two reference experiments, i) without light irradiation in the presence of catalyst, and ii) with light irradiation in the absence of catalyst should be done for comparison purposes. Composite to be collected under gravity filtration and dried under ambient conditions overnight before recycling for subsequent catalytic cycles. Each cycle under solar irradiation to be performed parallel to a control in the dark, administering the same recycling procedure. Hydroxyl radicals (OH*) produced during photocatalysis should be estimated using terephthalic acid as a probe molecule and an excitation wavelength of 315 nm. This method relies on the fluorescence signal at 425 nm of 2-hydroxyterephthalic acid.
[0167] In this method, the nanoparticles are tested in situ in the composite with the MOF. For strict adherence to the definition of the relative photonic efficiency r of the nanoparticles, the nanoparticles can be tested in an air-equilibriated aqueous dispersion, without MOF encapsulant. Where the nanoparticles are provided in the form of a composite with MOF, the nanoparticles can be isolated by digesting the MOF, e.g. at low pH. In the cases of the MOF being ZIF-8, a pH below 4-5 is suitable.
[0168] For further strict adherence to the definition of the relative photonic efficiency .sub.r of the nanoparticles, the 1.010.sup.5 M aqueous solution of dye (pH 7) can be replaced with 200 M phenol.
[0169] Further Experimental Work
[0170] We report here some additional experimental work that has been carried out to demonstrate further compositional embodiments. Specifically, the following materials were synthesised:
[0171] CdSe@ZIF-8.sub.mono
[0172] Au@ZIF-8.sub.mono
[0173] (PdO/TiO.sub.2)@ZIF-8.sub.mono
[0174] ((Au@PdO)/TiO.sub.2)@ZIF-8.sub.mono
[0175] Pd@HKUST-1 .sub.mono
[0176] CdSe@ZIF-8.sub.mono was synthesised by adapting the synthesis method for SnO.sub.2@ZIF-8.sub.mono disclosed above, the adaptation being the use of CdSe nanoparticles.
[0177] Au@ZIF-8.sub.mono was synthesised by adapting the synthesis method for SnO.sub.2@ZIF-8.sub.monodisclosed above, the adaptations being the following: Synthesis of Au nanoparticles (NP): HAuCl.sub.4.3H.sub.2O (7.88 mg, 0.02 mmol) and trisodium citrate (5.88 mg, 0.02 mmol) were dissolved in DI water (80 mL) and mixed vigorously.
[0178] An ice-cold solution of NaBH.sub.4 (9.08 mg, 0.24 mmol) in DI water (2.4 mL) was rapidly injected, causing the solution to turn from pale yellow to bright red/purple. The solution was mixed for 30 seconds at RT before PVP (10 k) (0.5 g) was added and mixed for a further 30 min. The water was removed under vacuum until 2 mL remained. The purple solution was diluted with distilled ethanol (18 mL).
[0179] For (PdO/TiO.sub.2)@ZIF-8.sub.mono, Pd/TiO.sub.2 nanoparticles were synthesized as follows: Stearic acid (0.84 g, 2.95 mmol) was dissolved in a solution of ethanol (80 mL) and DI water (20 mL) at 85 C. under rapid stirring. Pd(acac).sub.2 (0.03 g, 0.1 mmol) was added and the resulting yellow solution was heated under reflux for 4 hours yielding a black solution. A solution of Ti(OBu).sub.4 (0.4 mL, 1.17 mmol) in ethanol (2 mL) was added dropwise to the rapidly mixing solution. The solution was maintained at reflux for a further 2 hours before being cooled to room temperature. The solution was collected under cebtrifugation (5.5 k RCF, 10 min) and washed in alternating water/ethanol (1:7, 240 mL) and ethanol (240 mL) solutions. The resulting NPs were suspended in ethanol (20 mL) and dried under vacuum overnight before being heated in a furnace at 500 C. for 3 hours, yielding a brown solid.
[0180] For ((Au@PdO)/TiO.sub.2)@ZIF-8.sub.mono, Au@PdO nanoparticles were first formed as follows: HAuCl.sub.4.3H.sub.2O (0.02 g, 0.05 mmol) was dissolved in DI water (2.5 mL) under sonication to give solution A. Na.sub.2PdCl.sub.4 (0.015 g, 0.05 mmol) was dissolved in DI water (2.5 mL) under sonication to give solution B. Solution A and B were mixed together and PVP(40 k) (0.067 g) was added. Under rapid stirring a solution of ascorbic acid (0.07 g, 0.04 mmol) in DI water (0.67 mL) was quickly injected, causing a colour change from bright orange to dark brown. The solution was sonicated for 5 mins before being left to rapidly mix for a further 6 hours at RT. The solution was centrifuged (5.5 k RCF, 20 min.) to obtain a black/brown solid which was washed with DI water (340 mL). The resulting NPs were dried under vacuum or re-suspended in DI water (20 mL) and sonicated for 30 mins.
[0181] Next, Au@PdO/TiO.sub.2 nanoparticles were formed as follows: The Au@PdO NP aqueous suspension (20 mL) was added to a solution of stearic acid (0.84 g, 2.95 mmol) in ethanol (80 mL) at RT. Under rapid stirring a solution of Ti(Obu).sub.4 (0.4 mL, 1.17 mmol) in ethanol (2 mL) was added dropwise. The resulting grey mixture was heated to 115 C. over 10 mins and maintained at this temperature for 2 hours. The solution was cooled to RT and washed in alternating water/ethanol (1:7, 240 mL) and ethanol (240 mL) solutions before being dried under vacuum. The resulting grey powder was heated in a furnace at 500 C. for 3 hours.
[0182]
[0183]
[0184]
[0185]
[0186] While the invention has been described in conjunction with the exemplary embodiments described above, many equivalent modifications and variations will be apparent to those skilled in the art when given this disclosure. Accordingly, the exemplary embodiments of the invention set forth above are considered to be illustrative and not limiting. Various changes to the described embodiments may be made without departing from the spirit and scope of the invention.
[0187] All references referred to above and/or listed below are hereby incorporated by reference.
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