Shuhei
Fujita
a,
Kazunori
Kadota
b,
Atsushi
Koike
c,
Hiromasa
Uchiyama
b,
Yuichi
Tozuka
b and
Shunsuke
Tanaka
*ad
aDepartment of Chemical, Energy, and Environmental Engineering, Faculty of Environmental and Urban Engineering, Kansai University, Suita, Osaka 564-8680, Japan. E-mail: shun_tnk@kansai-u.ac.jp; Web: https://wps.itc.kansai-u.ac.jp/sepsyseng/
bDepartment of Formulation Design and Pharmaceutical Technology, Faculty of Pharmacy, Osaka Medical and Pharmaceutical University, Takatsuki, Osaka 569-1094, Japan
cDepartment of Pathobiochemistry, Faculty of Pharmacy, Osaka Medical and Pharmaceutical University, Takatsuki, Osaka 569-1094, Japan
dCollaborate Research Center of Engineering, Medicine and Pharmacology (CEMP), Organization for Research and Development of Innovative Science and Technology (ORDIST), Kansai University, Suita-shi, Osaka 564-8680, Japan
First published on 16th February 2024
Herein, we propose a simple and fast synthetic strategy for preparing highly crystalline γ-cyclodextrin-based metal–organic frameworks (solid yield 100%). This is the first method that allows metal–organic frameworks with high surface areas to be synthesised without a washing step.
The pursuit of commercial availability of MOFs is essential to advance the social implementation of MOFs in biochemical, pharmaceutical and food engineering. Among the most important challenges are the limited availability and high cost of commercially available MOFs and, above all, the difficulty of scaling up synthesis in a cost-effective manner while maintaining product quality. The cost of MOFs depends on the raw material costs (ligands, metal sources and solvents) and the manufacturing process (product recovery by filtration and other means, washing, drying, forming and processing), including capital investment, process energy, utilities and labor costs.9,10 To address process simplification and cost reduction, various synthesis methods have been demonstrated, including solvothermal, hydrothermal, microwave-assisted,11,12 sonochemical,13,14 microfluidic,15,16 aqueous solution,17,18 spray-drying19–22 and mechanochemical methods.23–27 To date, the most conventional and common method for obtaining CD-MOF crystals is the vapor diffusion method.7,8 In the vapor diffusion method, an aqueous solution of a metal salt and γ-CD in an appropriate ratio is placed in a glass container and left for several days under methanol diffusion. CD-MOFs consisting of K+, Rb+ and Cs+ have been successfully synthesized by methanol diffusion into an aqueous solution containing one equivalent of γ-CD and eight equivalents of each metal salt for a week.28,29 Although the vapor diffusion method is reliable and reproducible, it is time-consuming and requires solubility of the ligand, which limits its practical application for MOF production. Aqueous solution and mechanochemical methods have the potential advantages of mass production, high yields and avoidance of large amounts of organic solvents and high temperatures. The mechanochemical method, a well-known technique in metallurgy and mineral processing, has expanded the scope of its application to MOF synthesis in the last decade, leading to exciting research and development.30,31 The key idea behind this synthetic method is to accelerate the chemical reaction by exerting mechanical stresses to solid starting materials, minimizing or even eliminating the use of solvents. However, note that an activation step, in which the solid product is washed with an organic solvent, is necessarily essential for MOF synthesis. The mechanochemical method (as well as aqueous solution method) is no exception to this rule.32
Nevertheless, the mechanochemical method is the most environmentally friendly methodology and is therefore expected to be an economically promising MOF production process. In this study, a mechanochemical method for CD-MOF was developed for the first time, in which the product washing step was eliminated.
The synthesis procedure is very simple and can be reproduced by anyone. γ-CD and the potassium source (KHCO3, CH3COOK, KOH, KCl or K2CO3) together with a small amount of ethanol were placed in a 250 mL zirconia milling jar containing 30 YTZ® balls. Typically, the molar ratio of mixture is γ-CD:
K+
:
ethanol = 1
:
2
:
0.04; the K+/CD ratio can be varied from 0.67 to 8 and the ethanol/CD ratio can be reduced to 0.0085. These were then milled at a rotation rate of 150 rpm for 5 min by using a planetary mill Pulverisette 6 (Fritsch Japan). The products were only dried under atmospheric pressure at 80 °C for 1 h. Since this method only involves milling and drying, the final product can be obtained in 100% solid yield.
Fig. 1 shows the PXRD patterns of the products prepared with mechanochemical treatment. KHCO3 was used as the K+ source in these syntheses. Surprisingly, the dried products of the mixture of CD, KHCO3 and ethanol showed diffraction peaks attributed to the (110), (200), (211) and (220) planes of the CD-MOF crystal at 2θ = 4.0, 5.6, 7.1 and 13.3°, respectively.7 The crystal structure of CD-MOF was confirmed by the Rietveld refinement. However, it was also found that some KHCO3 remained unreacted when the K+/CD ratio was higher than 4. On the other hand, without mechanochemical treatment, some KHCO3 remained unreacted and further unidentified by-products were formed, as shown in Fig. S1 (ESI).† Mechanochemical treatment for only 5 min dramatically improved the yield of CD-MOF. The PXRD patterns of CD-MOFs prepared with other potassium sources (CH3COOK, KOH, KCl and K2CO3) are shown in Fig. S2 (ESI).†
Our synthetic method allows the production of CD-MOF without the need for a washing step. As the washing step is not required, the addition of excess potassium sources, which are not necessary for the structural formation of CD-MOF, increases the amount of unreacted potassium. The stoichiometric ratio of the coordination reaction between K+ and γ-CD is K+/CD = 2. In conventional synthetic methods such as vapor diffusion and poor solvent crystallization, it is common to add excess K+ to γ-CD and it is essential that the unreacted potassium is removed by washing. Excess K+ is not completely removed by washing and the composition of CD-MOF, K+/CD, is usually larger than 2. In contrast, our method has resulted in the formation of a crystal structure of CD-MOF with K+/CD less than 2.
The thermogravimetric curves of KHCO3, γ-CD and CD-MOF are shown in Fig. 2. It is well known that the thermal stability of CD-MOF is lower than that of the raw material γ-CD. This is because the presence of the potassium source promotes the pyrolysis of organic material γ-CD. This is the reason why the thermogravimetric loss of CD-MOFs with low K+/CD ratios shifted towards higher temperatures. The weight loss of CD-MOFs increased with decreasing K+/CD ratios because potassium-derived substances remain as residues after pyrolysis. The thermogravimetric curves of CD-MOFs prepared with other potassium sources (CH3COOK, KOH and KCl) are shown in Fig. S3 (ESI).† The pyrolysis behaviour depends on the potassium source. Among them, CD-MOFs prepared with KCl have the highest thermal stability.
![]() | ||
Fig. 2 Thermogravimetric curves of γ-CD and CD-MOFs. CD-MOFs were prepared by wash-free mechanochemical synthesis with different K+/CD ratios using KHCO3. |
The nitrogen adsorption/desorption isotherms of unwashed CD-MOFs are shown in Fig. 3. Table 1 shows the BET area and total pore volume of CD-MOFs. The original γ-CD is non-porous as it does not adsorb nitrogen at 77 K. In contrast, the products obtained by the reaction of γ-CD with potassium sources (KHCO3, CH3COOK, KOH, KCl or K2CO3) in this study could adsorb nitrogen and have relatively high BET areas, as shown in Fig. S4 (ESI).† As the K+/CD ratio increased from 0.67 to 2, the BET area of CD-MOF increased, reaching a maximum at K+/CD = 2, and decreased as the K+/CD was further increased. The lower BET area in the case of low potassium source addition is due to a low degree of crystallization. On the other hand, the low BET area in the case of excess potassium source addition is due to the presence of the unreacted potassium source. Since the stoichiometric composition of CD-MOF prepared using KHCO3 is K2(C48H80O40)(HCO3)2, it is reasonable that the BET area reached the maximum at K+/CD = 2. CD-MOF prepared at K+/CD = 2 by wash-free mechanochemical synthesis has a high BET area (906 m2 g−1) comparable to that prepared by the conventional vapor diffusion method (803 m2 g−1). To verify the necessity of the washing step, the nitrogen adsorption/desorption isotherm of the washed sample is shown in Fig. S5 (ESI).† The product washed after mechanochemical treatment had a reduced BET area (368 m2 g−1). This supports that the high crystallinity of the CD-MOF is obtained by wash-free mechanochemical synthesis. This is highly correlated with the high diffraction intensity result of the XRD pattern, as shown in Fig. 1. On the other hand, as the K+/CD ratio decreased, the diffraction intensities attributed to the crystal structure of CD-MOF became smaller, and the BET area of CD-MOF decreased accordingly. In particular, the BET area of CD-MOF prepared with K+/CD = 0.67 is low (143 m2 g−1), suggesting low crystallinity. It is estimated that the reduced BET area corresponds to the amorphous fraction. It has already been reported that even if the structure of CD-MOF is amorphous, it has potential applications as a drug carrier.21,22 The lack of potassium (especially under conditions of K+/CD < 1) causes defects in the CD bonds, resulting in reduced crystallinity, as shown in Scheme 1.
![]() | ||
Fig. 3 N2 adsorption/desorption isotherms of CD-MOFs prepared by wash-free mechanochemical synthesis. Before the measurements, the samples were degassed at 50 °C under vacuum for 6 h. |
Potassium source | K+/CD | S BET /m2 g−1 | V total /cm3 g−1 |
---|---|---|---|
a BET area. b Total pore volume. c Product washed after mechanochemical treatment. d CD-MOF prepared at K+/CD = 8 by the vapor diffusion method according to the literature.7 e CD-MOF-1 reported in the literature.7 Note that the activation conditions before N2 adsorption measurements are different. f Original γ-CD. | |||
KHCO3 | 8 | 527 | 0.253 |
KHCO3 | 6 | 574 | 0.339 |
KHCO3 | 4 | 655 | 0.362 |
KHCO3 | 2 | 906 | 0.373 |
KHCO3 (washed)c | 2 | 368 | 0.173 |
KHCO3 | 1.5 | 600 | 0.306 |
KHCO3 | 1 | 415 | 0.238 |
KHCO3 | 0.67 | 143 | 0.137 |
KCl | 2 | 878 | 0.438 |
KOH | 2 | 698 | 0.401 |
CH3COOK | 2 | 631 | 0.370 |
K2CO3 | 2 | 30.0 | 0.057 |
(Vapour diffusion method)d | 803 | 0.322 | |
(CD-MOF-1)e | 1220 | 0.48 | |
(γ-CD)f | 1 | 0.009 |
![]() | ||
Scheme 1 Schematic illustration of the barrel-like structure of CD linked by K+. Note that K+ at the widest bilge of the barrel is shared with the head of the adjacent barrel. |
There is a significant difference in the size of the crystals compared to the conventional method. While the vapor diffusion method usually yields crystals of several hundred micrometers, the particle sizes obtained by wash-free mechanochemical synthesis are from submicrons to a few micrometers, as shown in Fig. S6 (ESI).† It has been reported that the particle sizes of submicrons to a few micrometers are suitable for drug delivery systems, especially for transpulmonary formulations.21,33
This study demonstrates that CD-MOFs with high BET area can be synthesized using any type of potassium source by mechanochemical synthesis without the need for a washing step. Although the synthesis of CD-MOFs using KCl or CH3COOK instead of KOH has been reported, in all cases reported so far, the synthesis takes a long time and/or requires additives to obtain the product.34–38 Conventional synthesis methods invariably require a process to wash the products. In contrast, in our method, CD-MOFs can be synthesized in just over an hour. Furthermore, as the third component is a very small amount of ethanol, it can be easily removed by drying the product at a relatively low temperature. As shown in Fig. S7 (ESI),† drying of the product at 60 °C for 1 h is sufficient for activation.
CD-MOFs can be successfully synthesized even when the ethanol/CD ratio is reduced to 0.023 (the standard ethanol/CD ratio is 0.04). However, at lower ratios, the potassium source remains unreacted, as shown in Fig. S8 (ESI).† The role of the third component, ethanol, is therefore to facilitate mass transfer and mixing between γ-CD and the potassium source.24,25 Under conditions with ethanol/CD ratio above 0.023, CD-MOFs can be synthesized even when the mechanochemical reaction time is reduced to 5 min, as shown in Fig. S9 (ESI).† This method can achieve both structure formation and drug delivery of CD-MOFs simultaneously. Furthermore, our method can achieve both structure formation of CD-MOF and drug inclusion in its pores simultaneously by adding a drug as the fourth component. In this study, an antitubercular drug levofloxacin hydrate was used as a model. Levofloxacin has hydrophilic nature and can be encapsulated in the hydrophilic pores of CD-MOF. As a demonstration, levofloxacin could be successfully encapsulated in CD-MOF at 15.5 wt%, as shown in Fig. S10 (ESI).† Since the solubility of levofloxacin in ethanol is 9 mg mL−1 at 25 °C, levofloxacin just adhering to the surface of CD-MOF particles can be easily washed off with ethanol. In contrast, CD-MOF is insoluble in ethanol and its structure is stable against ethanol. Levofloxacin was not eluted from the levofloxacin-encapsulated CD-MOF with ethanol, strongly indicating that levofloxacin is confined within the pores of the CD-MOF. This inclusion amount is approximately double the amount previously encapsulated by our group using the spray-drying method. One of the reasons for this difference is that CD-MOF prepared by wash-free mechanochemical synthesis has a much larger BET area than that prepared by the spray-drying method (∼94.1 m2 g−1).21,22
Furthermore, in this study, an antifungal drug clotrimazole was successfully encapsulated in CD-MOF at 14.6 wt% as an insoluble model drug. Due to solubility issues, it is difficult to simultaneously encapsulate both soluble and insoluble drugs in CD-MOF using liquid phase methods, including spray-drying. On the other hand, wash-free mechanochemical synthesis, which only involves milling solid mixtures, can synthesize MOF-DDS without dissolving drugs in solvent, thus enabling simultaneous encapsulation of both soluble and insoluble drugs in CD-MOF. However, when levofloxacin and clotrimazole were added simultaneously, their content in the CD-MOF carrier (levofloxacin; 11.1 wt%, clotrimazole; 13.4 wt%) was lower than those prepared by adding each drug alone.
It is important to understand the potential cytotoxicity of CD-MOF carriers prepared by the novel method, wash-free mechanochemical synthesis. Although several groups have reported on the cytotoxicity of CD-MOFs, most of these studies have been conducted using Caco-2, the small intestine cells. Few studies have examined the toxicity of MRC-5, lung cells, or A549, alveolar cells. In commonly reported cases, cytotoxicity assessments have been carried out at concentrations up to 1 mg L−1,33,39,40 whereas in this study, cytotoxicity assessments were carried out up to ultrahigh concentrations of up to 10 g L−1, as shown in Fig. 4. Incidentally, CD-MOFs prepared using KOH, KHCO3, CH3COOK and KCl showed pH 11.64, 11.24, 7.22 and 6.77 at 10 g L−1 concentration in aqueous solution, respectively. Even when the concentration of CD-MOF carriers reached 10 g L−1, the viability of all three cells remained above 90%, indicating superior biocompatibility. The low cytotoxicity of CD-MOF carriers could be attributed to the non-toxic and biodegradable nature of γ-CD and potassium sources used. CD-MOFs prepared by wash-free mechanochemical synthesis are therefore safe for oral and transpulmonary administration.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3mr00006k |
This journal is © The Royal Society of Chemistry 2024 |