Manuel
Otter
a,
Gabriel
Partl
b,
Michael
Noisternig
c and
Rania
Bakry
*a
aInstitute of Analytical Chemistry and Radiochemistry, Leopold-Franzens-University Innsbruck, Innrain 80–82, 6020 Innsbruck, Austria. E-mail: rania.bakry@uibk.ac.at; Fax: +43 512 507 57399; Tel: +43 512 507 57308
bInstitute of General, Inorganic and Theoretical Chemistry, Leopold-Franzens-University Innsbruck, Innrain 80-82, A-6020 Innsbruck, Austria
cInstitute of Pharmacy, Pharmaceutical Technology, Leopold-Franzens-University Innsbruck, Innrain 52c, A-6020 Innsbruck, Austria
First published on 13th January 2022
Porous layered monolithic substrates of poly(butyl methacrylate-co-ethylene dimethacrylate) were synthesized via UV initiated free radical polymerization in the presence of fluoroponytailed ionic liquids as co-porogenic constituents. The effects of the type and the amount of selected fluorous ionic liquids on various properties of the monolithic support, e.g. porosity, specific surface area and chromatographic performance, in particular for their usability in reversed phase TLC, were examined. Porosity was characterized by means of mercury porosimetry and scanning electron microscopy. The monolithic stationary phases with different layer thickness were successfully applied in the separation of three curcuminoids, namely curcumin, demethoxycurcumin and bisdemethoxycurcumin. Relative retention factor, theoretical plates and resolution were used for the evaluation of the monolithic support's performance. To verify the feasibility of the monoliths, the method was employed for the discrimination between the plant species Curcuma longa and Curcuma xanthorrhiza.
Porogens, pore generating solvents, are the most important components of the polymerization mixture affecting the surface area, porosity and morphology of the resulting monolithic structure. The porogens used for the preparation of porous monoliths by in situ free radical polymerization mostly consist of a mixture of solvating and non-solvating diluents. Solvating porogens are mostly responsible for the generation of micro-/mesopores, whereas non-solvating types are attributed to generate macropores.4 The choice of porogen depends on the polarity and solubility of monomers, polymer and co-porogens. Owing to the different characteristics of porogens, they generate different pore architectures within the polymeric structure. The solvating porogens are miscible with the monomers as well as the initially formed oligomers, resulting in late-stage phase separation at higher conversion of monomer to polymer. As a result, a scaffold with interconnected individual microglobules is formed. Conversely, non-solvating porogens are responsible for early-stage phase separation at lower conversion, due to their poor miscibility in the polymerization system. This process causes the aggregation of the microglobules and the formation of a scaffold with low surface area.
Organic solvents and organic polymers are commonly used porogens.5 The main factors governing the choice of suitable porogens are their molecular size, alkyl chain length and solubility profiles.6 Most organic liquids can be used in monolith fabrication, even volatile solvents can be employed in the preparation through photoinitiated polymerization. During the last decade, ionic liquids (ILs) attracted growing attention as porogens or co-porogens.7–9 The most widely used porogen ILs are 1-butyl-3-methylimidazolium salts, in particular with BF4−, PF6−, HSO4− anions.5 They offer numerous advantages, including negligible volatility as well as highly tuneable solubility profiles. ILs may even significantly enhance the polymerization rate, through acceleration of the rate of monomer propagation.10 Expectedly, the presence of ILs also affects the morphology of the monolith by altering swelling and shrinking behaviour of the monolith. However, the benefit of ILs on the chromatographic separations in thin layer format is not reported.
In our previous work, we demonstrated the thin layer chromatographic separation of peptides and proteins on poly(butyl methacrylate-co-ethylene dimethacrylate) (poly(BMA-EDMA)) monoliths followed by MALDI-TOF MS detection. The monoliths were prepared by photoinitiated free radical polymerization using dodecanol and cyclohexanol as porogens.11 The resulting monoliths were successfully used for the separation of peptides and proteins. However, their application for the separation of small molecules was not satisfactory. Svec's group improved the efficiency for the separations of small molecules by hypercrosslinking poly(4-methylstyrene-co-chloromethylstyrene-co-divinylbenzene) via Friedel–Crafts alkylation.12 Maksimova et al., studied the separation low molecular weight dyes and dinitrophenol amino acids using a series of methacrylate based monolithic support. Several functional monomers were used including glycidyl methacrylate, butyl methacrylate, aminoethyl methacrylate, 2-hydroxyethyl methacrylate and 2-cyanoethyl methacrylate.13 Later on, Yin et al. demonstrated the application of macroporous poly HIPE monolithic layers based on poly(styrene-butyl acrylate-divinylbenzene) for the identification of Chinese herbal medicinal components.14 Recently, Korzhikova-Vlakh et al. summarizes the current achievement on the application of microporous polymer monolithic layers for thin layer chromatography.15
In this work, we focused on the development of planar monoliths with optimized porosity for the separation of small molecules based on poly(BMA-EDMA) using specific ILs, mainly fluoroponytailed room temperature ILs (FILs), as co-porogens. The selected FILs were synthesized using efficient and cost-effective procedures developed by Schottenberger's group.16,17 The monolithic supports were prepared using ternary porogenic solvents consisting of cyclohexanol, 1-dodecanol or 1-decanol, and 2-(1H,1H,2H,2H-perfluorooctylthio)-1-methylimidazolium with varying counter ions (Fig. 1). The effect of FILs concentration on the porous structure of monolithic support was studied. The resulting monoliths were morphologically characterized by scanning electron microscopy and mercury porosimetry. The performance of the developed monoliths was assessed for their suitability to separate three curcuminoids by thin layer chromatography. Furthermore, the monolithic plates were applied for discrimination between two Curcuma species.
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Fig. 1 Chemical structure of the utilized FILs, 2-(1H,1H,2H,2H-perfluorooctylthio)-1-methylimidazolium: iodide (a), triflimide (b), perfluoro-3,6,9-trioxatridecanoate (c). |
Monolith | Monomer | Crosslinker | Porogenic solvent | |||
---|---|---|---|---|---|---|
BMA (%w/w) | EDMA (%w/w) | 1-Decanol (%w/w) | 1-Dodecanol (%w/w) | Cyclohexanol (%w/w) | FILs (%w/w) | |
a Iodide. b Triflimide. c Perfluoro-3,6,9-trioxatridecanoate. | ||||||
I | 24.0 | 16.0 | 40.0 | 20.0 | ||
II | 24.0 | 16.0 | 40.0 | 10.0 | 10.0a | |
III | 24.0 | 16.0 | 40.0 | 10.0 | 10.0b | |
IV | 24.0 | 16.0 | 40.0 | 10.0 | 10.0c | |
V | 18.0 | 12.0 | 46.7 | 11.7 | 11.6a | |
VI | 24.0 | 16.0 | 40 | 10.0 | 10.0a | |
VII | 24.0 | 16.0 | 40 | 20.0 |
![]() | (1) |
![]() | (2) |
![]() | (3) |
As mentioned introductorily, the effect of FILs on the pore morphology of the monolithic layers can vividly be elucidated by microscopy. Fig. 2I shows the SEM images of porous structure of monoliths with conventional (generic) composition exhibiting its typical porous features (monolith I). However, the monoliths (II–IV) prepared using 10% w/w FILs as co-porogen with 40% w/w 1-decanol and 10% cyclohexanol exhibit denser porous structures (Fig. 2II–IV). The denser porous structure can be attributed to the good solvating properties of the FILs towards the monomers. Therefore, the local concentration of monomers in FILs is higher than that in the precipitated, insoluble “gel-like” species (nuclei), leading to individualized small globules. Additionally, the large number of nuclei competing for the remaining monomers results in high numbers of small globules that aggregate with small pores, as can be seen in Fig. 2II–IV.19 Additionally, it can be noticed that changing the anion of the FILs has a remarkable effect on pore architecture and polymeric backbone density. The use of the triflimide FIL causes a non-uniform monolithic structure, in contrast to the monoliths prepared utilizing iodide and perfluoro-3,6,9-trioxatridecanoate FILs. However, the flow channels are wider with triflimide and perfluoro-3,6,9-trioxatridecanoate (monolith III and IV), compared to monolith II prepared with iodide. Furthermore, decreasing the ratio of monomer to porogen from 40% to 30%, as is the case for monolith V, resulted in wider flow channels with larger globule size (Fig. 2V). On the other hand, the incorporation of 1-dodecanol instead of 1-decanol (monolith VI) into the monomeric mixture effected a remarkable change in morphology (Fig. 2II and VI). 1-Dodecanol has less solvating power for the polymer chains in comparison to 1-decanol, resulting in earlier phase separation. As can be noticed from Fig. 2VI, the porous scaffold is less dense and possesses larger globule sizes with homogenous through-pores and polymer clusters, in comparison to monolith II. Consequently, the change in morphology was reflected in the changes in the specific surface area of the monoliths. The utilization of the FILs as co-porogens resulted in approximately 100% increase in specific surface area, since the nuclei retain their individuality. Monolith VII, prepared without FILs, possesses a surface area of 16 m2 g−1. Conversely, the use of 10% FILs resulted in monoliths with surface areas up to 33 m2 g−1 (monolith VI). This increase in the surface area can be attributed to the increase of clusters with smaller size. As mentioned before, the presence of the ILs accelerates the polymerization rates accompanied with late phase separation, which would produce microglobules.10
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Fig. 2 Scanning electron microscope images of monoliths (VI and VII) prepared according to composition summarized in Table 1. |
Furthermore, the influence of the incorporation of FILs as co-porogens on the pore size distribution of the developed monolithic supports was examined using mercury porosimetry. Pore size distribution indicates the accessible fraction of total pore volume. As can be shown in Fig. 3, both monolithic plates VI and VII possess monomodal pore size distribution. Monolith VI, prepared using 10% iodide FIL, 1-dodecanol and cyclohexanol as porogens, displays a comparatively broad pore size distribution profile with total intrusion volume of 1.62 ml g−1 and average pore radius of 0.360 μm, resulting in a total porosity of 63.0%. However, monolith VII, prepared without FILs, exhibits a pore size distribution with total intrusion volume of 1.81 ml g−1 at a pore radius of 1.5 μm, with a total porosity of 65.7% (Fig. 3).
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Fig. 3 Pore size distribution of poly(BMA-EDMA) monoliths VI (with 10% FIL-iodide) and VII (without FIL). |
FT-IR was utilized to confirm that the FILs were not incorporated into the formed monolith. The FT-IR spectrum of e.g. monolith VI did not show any evidence towards the presence of any FIL-specific IR bands. The spectra of plates I and VI are identical in regard to the polymer's characteristic absorption bands (ESI1†).
(Zf)2 = kt | (4) |
Table 2 summarizes the velocity constant of the developed monoliths with 150 μm thickness using ACN/H2O (60/40) with 0.1% TFA. The plates are used for reasonable distances ranging from 30–60 mm. Monolith I exhibits a velocity constant of approximately 2.67 mm2 s−1, whereas monoliths II–IV show velocity constants ranging from 0.49 to 1.30 mm2 s−1. The results are following SEM images, whereas monolith I demonstrates wider flow-channel compared to monoliths II–IV. Monolith V, prepared with only 30% monomer content, possesses a highly porous scaffold and shows the highest permeability with a velocity constant of 6.08 mm2 s−1.
Monolith | Methylene blue | Methyl red | R s | Velocity constant mm2 s−1 | ||
---|---|---|---|---|---|---|
R f | Spot width mm | R f | Spot width mm | |||
I | 0.88 | 0.2 | 0.77 | 0.35 | 0.40 | 2.66 |
II | 0.66 | 0.4 | 0.32 | 0.55 | 0.72 | 0.49 |
III | 0.87 | 0.6 | 0.70 | 0.55 | 0.29 | 0.83 |
IV | 0.93 | 0.5 | 0.58 | 0.5 | 0.70 | 1.29 |
V | 0.89 | 0.18 | 0.65 | 0.3 | 1.13 | 6.08 |
VI | 0.87 | 0.2 | 0.60 | 0.2 | 1.20 | 2.01 |
Furthermore, to evaluate the feasibility of the developed plates for the separation of small molecules, curcumin (CurI), demethoxycurcumin (CurII) and bisdemethoxycurcumin (CurIII) are selected as model analytes (ESI2†). Firstly, the mobile phase applied for chromatographic separation was optimized. Different mobile phase compositions were tested, using monoliths VI and VII, namely ACN/H2O 60/40, CH2Cl2 and CHCl3 to obtain good resolution and reproducible separation. With ACN/H2O, no separation could be achieved on both monoliths. Using CH2Cl2 and CHCl3, the three curcuminoids could not be separated on monolith VII, prepared without FILs. A yellow smear was obtained for CurI und CurII. However, employing monolith VI good separation could be obtained, with CHCl3 giving superior results in terms of resolution and spot width. These results showed that, the incorporation of FILs in monolith synthesis improved notably of the separation efficiency of the monolithic plates.
Table 3 summarizes the data obtained by using CHCl3 and CH2Cl2 as mobile phases on monolith VI. For example, the spot width for curcumin using CHCl3 was 1.7 mm, whereas with CH2Cl2 it was 6.7 mm. The plates are used for distances and speeds ranging from 3–6 cm in 8–9 min, since longer distances resulting in impaired separation because of diffusion in the layer. The highest number of theoretical plates, namely 2539.69, was obtained with CurI using CHCl3 as mobile phase.
Mobile phase | R f (±SD) | Spot width (mm) | N | R s |
---|---|---|---|---|
Analyte | ||||
CHCl 2 | ||||
CurI | 0.18 ± 0.006 | 3.2 | 336.91 | 5.67 |
CurII | 0.67 ± 0.137 | 2.6 | 1878.10 | 1.41 |
CurIII | 0.88 ± 0.002 | 6.7 | 375.05 | |
CHCl 3 | ||||
CurI | 0.17 ± 0.048 | 2.4 | 209.02 | 5.85 |
CurII | 0,65 ± 0.044 | 1.7 | 1666.44 | 3.33 |
CurIII | 0.87 ± 0.036 | 1.6 | 2539.69 |
Fig. 4 demonstrates a representative separation of curcuminoids standard solution on monolith VI using CHCl3 as mobile phase. The plates were visualized using UV light with a wavelength of 365 nm. However, since clear identification of spots is not possible by visualization or staining, the spots were scraped off the TLC plate and extracted with methanol. The extracted curcuminoids were loaded on the MALDI target combined with DHB matrix. MALDI-MS offers a soft ionization technique for a fast and simple method for identification of the separated spots. MALDI-MS spectra of the 3 curcuminoids shown in Fig. 4(b–d) indicate the good separation behaviour of the monolithic plates. As can exemplified by Fig. 4b, the m/z of 369 Da clearly corresponds to the [M + H]+-peak of CurI. In Fig. 4c, the m/z of 339 Da correlates to CurII, and the m/z of 309 Da corresponds to CurIII (Fig. 4d). Coupling of TLC and MALDI-MS is one of the promising hybrid analytical methods. It opens broad possibilities regarding identification, screening, methods development for the analysis of wide range of analytes.24
The effect of monolithic layer thickness on the chromatographic separations of curcuminoids was investigated. Several monolithic plates were prepared with a thickness between 25 and 200 μm. Using monolithic plates with a thickness of 25 and 50 μm, no separation of the three curcuminoids could be obtained due to the low capacity of the monolith. However, the good separation was obtained using a monolithic layer with 150 μm thickness. Additionally, the reusability of the monolithic plates was examined by repeated use after washing with ethanol and drying at 60 °C. A reproducible separation of the three curcuminoids was achievable even after five times.
Plant | Origin | CurI (±SD) | CurII (±SD) | CurIII (±SD) |
---|---|---|---|---|
Cur.L.: Curcuma Lunga; Cur.Xan.: Curcuma Xanthorriza; curI: bisdemethoxycurcumin; CurII: demethoxycurcumin; CurIII: curcumin. | ||||
Cur.L.1 | Sleman | 0.12 ± 0.032 | 0.62 ± 0.093 | 0.85 ± 0.014 |
Cur.L.2 | Playen | 0.21 ± 0.001 | 0.66 ± 0.045 | 0.90 ± 0.001 |
Cur.Xan.1 | Naggulan | 0.65 ± 0.035 | 0.85 ± 0.042 | |
Cur.Xan.2 | Girimulyo | 0.67 ± 0.020 | 0.85 ± 0.060 |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/d1an02005f |
This journal is © The Royal Society of Chemistry 2022 |