Heeju
Song
a,
Yeonjin
Hong
a and
Hyungseok
Lee
*ab
aDepartment of Smart Health Science and Technology, Kangwon National University, Chuncheon, Republic of Korea. E-mail: ahl@kangwon.ac.kr; Tel: +82 33 250 6309
bDepartment of Mechanical and Biomedical, Mechatronics Engineering, Kangwon National University, 1, Kangwondaehak-gil, Chuncheon-si, Gangwon-do, Republic of Korea
First published on 3rd December 2024
Despite considerable animal sacrifices and investments, drug development often falters in clinical trials due to species differences. To address this issue, specific in vitro models, such as organ-on-a-chip technology using human cells in microfluidic devices, are recognized as promising alternatives. Among the various organs, the human small intestine plays a pivotal role in drug development, particularly in the assessment of digestion and nutrient absorption. However, current intestine-on-a-chip devices struggle to accurately replicate the complex 3D tubular structures of the human small intestine, particularly when it comes to integrating a variety of cell types effectively. This limitation is primarily due to conventional fabrication methods, such as soft lithography and replica molding. In this research, we introduce a novel coaxial bioprinting method to construct 3D tubular structures that closely emulate the organization and functionality of the small intestine with multiple cell types. To ensure stable production of these small intestine-like tubular structures, we analyzed the rheological properties of bioinks to select the most suitable materials for coaxial bioprinting technology. Additionally, we conducted biological assessments to validate the gene expression patterns and functional attributes of the 3D intestine-on-a-chip. Our 3D intestine-on-a-chip, which faithfully replicates intestinal functions and organization, demonstrates clear superiority in both structure and biological function compared to the conventional 2D model. This innovative approach holds significant promise for a wide range of future applications.
The digestive system encompasses organs responsible for ingestion and excretion.6 Within this system, the gastrointestinal tract includes a series of interconnected organs forming a continuous tube that serves as the pathway for food from the mouth to the anus. The human small intestine, situated between the stomach and large intestine, exhibits distinct internal layers, including the intestinal lumen, mucosa, submucosa, muscularis propria, and serosa. The intestinal lumen serves as the conduit for ingested substances, while the mucosal layer features specialized villi responsible for nutrient absorption. Nutrients are transported through the villi via blood vessels and lacteals within the submucosal layer. The muscularis propria and serosal layers contain specific muscle types that facilitate peristalsis and provide tissue protection, respectively. The widespread use of oral medications, attributable to their ease of manufacture and distribution,7 along with patients' adherence to medical prescriptions,8 underscores the critical importance of understanding drug absorption mechanisms in the small intestine. Consequently, developing an ideal in vitro intestinal model is imperative for advancing drug delivery optimization.
Two-dimensional (2D) transwell models have long been regarded as the predominant method for investigating intestinal physiology and function as conventional intestinal in vitro models. These models allow cells to be cultured under different conditions in two chambers separated by a porous membrane, enabling the analysis of the migratory properties of cells. Culturing Caco-2, an intestinal epithelial cell line, on transwell models yields outcomes that closely mimic the structure and function of native small intestinal epithelium.9 The function of the small intestine can be analyzed by applying reagents to the upper chamber where Caco-2 are cultured, followed by the analysis of samples from the lower chamber. Owing to their simplicity and ease of use, 2D transwell models are widely used at present as in vitro models. Considerable efforts have been made to improve these models by stacking different types of small intestinal cells in a single layer to mimic the structural characteristics of the small intestine or co-culturing different types of cells in a single layer.10,11 However, transwell models still have inherent limitations in the functional expression of Caco-2 cells owing to the constraints in accurately mimicking the native environment.12
Organ-on-a-chip is a three-dimensional (3D) platform fabrication technique incorporating microfluidic systems, enabling the culture of tissue-specific cells within an environment that mimics the conditions encountered in the human body.13 Microchannel platforms offer precise size control in laboratory settings, facilitate rapid fluid mixing, and provide economic advantages through minimal reagent usage.14 For example, the intestine-on-a-chip (IOC) features flexible silicon chambers positioned on both sides of a microchannel with a porous membrane in the center.15 Although the IOC successfully emulates the 2D microenvironment of the small intestine, its structural configuration deviates from that of the actual small intestine, which typically exhibits a long cylindrical shape with a hollow center. This aspect highlights a limitation in its design. To date, numerous in vitro intestinal models have been developed. However, none have successfully replicated the long, cylindrical structure of the actual small intestine, crucial for mimicking the 3D biological environment. Therefore, in this study, we engineered a 3D tubular structure designed to replicate the cylindrical morphology of the small intestine using extrusion-based coaxial bioprinting. To recreate a 3D environment, we attached intestinal epithelial cells to the inner surface of this biocompatible tubular structure to establish a more authentic intestinal epithelium. We also explored the integration of small intestinal smooth muscle cells and vascular endothelial cells into the structure using bioprinting technology. This innovative approach not only replicated the structural characteristics of the actual small intestine but also enabled the use of various cell types within the IOC system, thereby enhancing the model's functionality and paving the way for future applications in drug testing.
The hybrid cell line EA.hy926, resulting from the fusion of human umbilical vein endothelial cells (HUVECs) and A549, a thioguanine-resistant human lung carcinoma cell line, served as the selected vascular endothelial cell line in this study due to its distinctive endothelial characteristics. EA.hy926 were sourced from ATCC, USA, with accession number CRL-2922. The culture conditions and medium composition for EA.hy926 were identical to those used for Caco-2.
Human small intestine smooth muscle cells (HSISMC), sourced from Innoprot, Spain, under the trade name P10751, are primary cells isolated from healthy human small intestine. These cells were cultured in a smooth muscle cell medium (SMCM, with growth supplements, P60125; Innoprot, Spain). The cells from passages two to five were seeded at a density of 2 × 106 cells in 150 mm cell-culture dishes, and the medium was refreshed every other day.
When the cells reached confluence at 37 °C in a humidified atmosphere with 5% CO2 (BB15 CO2 Incubator, 51023121; Thermo Fisher, USA), a two-step detachment process was used. Initially, the cells underwent two rinses with 1× PBS (SM-P02-100, Solmate; GeneAll Biotechnology, Republic of Korea). The cells were then subjected to trypsin treatment (25300054, Gibco; Thermo Fisher, USA) for 2 min to facilitate detachment from the culture dish. The resulting cell suspension was transferred to a 50 mL conical tube (352070, Falcon; Corning, USA) containing 5 mL of the medium to neutralize the trypsin. The remaining cells in the dishes were incubated for an additional 2 min to ensure thorough collection. To ensure the collection of all remaining cells, 5 mL of the medium was spread across the dishes multiple times. The harvested cells were then transferred to the conical tube to the greatest extent possible. Finally, the collected cells were centrifuged at 800 RPM for 6 min in a centrifuge (1248R; Labogene, Republic of Korea) maintained at 4 °C.
Collagen sponge (derived from porcine skin, type I; PC-001; Dalim Tissen, Republic of Korea) was introduced into a solution of 17 mM acetic acid (1006-3705; Daejung Chemical & Metals, Republic of Korea) and stirred at 330 RPM for 6 h, forming a 1.5% (w/v) stock solution. Subsequently, the collagen stock solution was prepared proportionally to achieve a 1% (w/v) collagen bioink. This process included the addition of 10× PBS to one-tenth of the final solution volume and 1 M sodium hydroxide (S2018; Biosesang, Republic of Korea) to 1% (v/v) of the final solution volume for pH neutralization. The pH was adjusted in the range of 7.2–7.4 using minimal quantities of 1 M acetic acid and 1 M sodium hydroxide. The remaining solution was supplemented with DMEM, constituting four-fifths of the final solution volume. Lastly, cell pellets, along with the medium accounting for one-fifth of the final solution volume, were introduced to produce a 1% (w/v) collagen bioink containing cells. For the middle layer, a 1% collagen bioink with a cell density of EA.hy926 at 2 × 106 cells per mL.
A 4% (w/v) alginate bioink was prepared by dissolving alginic acid sodium salt powder (71238, Sigma-Aldrich; Merck, Germany) in 1× PBS. The mixture was stirred using a heating magnetic stirrer (SP88857105, Thermo Scientific; Themo Fisher, USA) at 140 °C and 440 RPM for 2 h, with a room temperature of 20 °C. The 4% (w/v) alginate bioink was mixed with a 1% (w/v) collagen bioink containing cells in a 1:1 ratio, resulting in a 2% (w/v) alginate–0.5% (w/v) collagen bioink with a cell density of HSISMC at 4 × 106 cells per mL.
To evaluate the printability of collagen-based bioinks in the context of pre-crosslinking treatments, we analyzed the storage and loss moduli for 1% collagen bioink during both heating and cooling phases. Similar to the gelatin bioinks, these experiments were conducted at a frequency of 1 Hz, and the resulting data were presented in terms of tan(δ), representing the ratio of the loss modulus to the storage modulus. Moreover, after establishing suitable preparation conditions for automated production, we scrutinized viscosity curves for collagen-based bioinks characterized by lower melting points. This examination aimed to affirm that the pre-crosslinking treatment rendered the collagen-based bioink attainable in a printable gel state, ensuring its suitability for use in the printing process.
The storage moduli of both alginate–collagen and collagen scaffolds, cultured in the incubator for 12 h, were determined to assess their structural stability. Sample preparation involved casting 1.5-mm-thick layers of alginate–collagen bioinks and collagen bioinks in 35 mm Petri dishes. The samples were subjected to several processing steps: 15 min in a 37 °C incubator, 10 min in a 10 °C cooling environment, 10 min in a 2% (w/v) calcium chloride solution (1098, Duksan Pure Chemicals, Republic of Korea), 5 min in 1× PBS, followed by a thorough wash with 1× PBS, and subsequent replenishment with fresh media. The storage moduli of these samples were measured under consistent shear strain conditions of 0.5% and angular frequencies ranging from 1 to 100 rad s−1.
For comparison, 12-well plate-sized transwell models (37012; SPL, Republic of Korea) were used as the control group. The seeding conditions involved using 500 μL of medium containing 1.25 × 105 cells of Caco-2 in the upper compartment and 1 mL of cell-free medium in the lower compartment. The medium in both compartments was changed every other day in equal volumes. In the dynamic culture system, a rocker (SHRK04DG; Ohaus, USA) was used for cultivation. For the dynamic culture models, a rocker was used to implement flow conditions of 4 °C and 10 RPM. These conditions were chosen to ensure even coverage on both sides of the culture and prevent detachment of the Caco-2 cells from the surface.
Type | Product name | Brand | Catalog number | Dilution |
---|---|---|---|---|
1st | ZO-1 monoclonal antibody (ZO1-1A12), Alexa Fluor™ 594 | Invitrogen | 33194 | 1:200 |
1st | Villin polyclonal antibody | Invitrogen | PA5-29078 | 1:200 |
1st | MUC2 polyclonal antibody | Invitrogen | PA5-103083 | 1:200 |
1st | Lysozyme polyclonal antibody | Invitrogen | PA5-16668 | 1:100 |
2nd | Goat anti-rabbit IgG (H + L), superclonal recombinant secondary antibody, Alexa Fluor 488 | Invitrogen | A27034 | 1:1000 |
Dye | DAPI (4′,6-diamidino-2-phenylindole, dihydrochloride) | Invitrogen | D1306 | 1:500 |
Dye | Alexa Fluor™ 488 phalloidin | Invitrogen | A12379 | 1:400 |
Gene | Target | Primer type | Primers (5′-3′) | Genebank accession |
---|---|---|---|---|
GAPDH | Housekeeping gene | Forward | TGGAAGGACTCATGACCACAG | NM_001357943.2 |
Reverse | TCCACCACTGACACGTTGG | |||
CYP3A4 | Metabolism | Forward | CCCACAAAGCTCTGTCCGAT | NM_001202855.3 |
Reverse | TATCATAGGTGGGTGGTGCC | |||
CD31 | Vascular endothelial cells | Forward | GTCCCTGATGCCGTGGAAA | NM_000442.5 |
Reverse | GGAGCAGGGCAGGTTCATAA | |||
ACTA2 | Smooth muscle cells | Forward | AGCGCAAATACTCTGTCTGG | NM_001406464.1 |
Reverse | CAGAGAGGAGCAGGAAAGTGT | |||
CTNND1 | Cell morphology | Forward | CTGGTAAGAGAAGTGAGTGGTG | NM_001085469.2 |
Reverse | CTAAAGTGAGAGGGGGCAATAC | |||
VIL1 | Microvilli found on the villous top | Forward | GCCTCGATGGAAGCAACAAA | NM_007127.3 |
Reverse | CGGTGAGAAAATGAGACCCTAC | |||
LYZ | Protective enzyme secreted in crypts | Forward | GCCAAATGGGAGAGTGGTTAC | NM_000239.3 |
Reverse | CCTGGGGTTTTGCCATCATTAC | |||
TJP1 | Barrier function | Forward | GGAGGGTGAAGTGAAGACAATG | NM_001330239.4 |
Reverse | CTGCTGGTTAGTATGTCTGTGG | |||
MUC2 | Mucus secretion | Forward | GCCCTCTAACAACTACTCCTCT | NM_002457.5 |
Reverse | GGTTTTCCAGAATCCAGCCAG |
In coaxial nozzle bioprinting, F-127 is frequently chosen as a material due to its favorable properties. However, it has certain limitations, particularly when it comes to encapsulating cells. One major issue is that F-127 can negatively affect cell viability, making it less ideal for applications where cell survival is critical.16 Additionally, even when used in bioprinting without cells, F-127 remains in a gel-like state at the typical cell culture temperature of 37 °C. This characteristic requires an extra step to remove the material after printing,17 which adds complexity to the overall process. Contrarily, the choice of gelatin bioink as a sacrificial material ensures uniform cell encapsulation and creates passageways without negatively impacting the Caco-2 until they adhere to the inner structure (Fig. 1(B)). Notably, gelatin bioinks can exhibit variations in viscosity due to cooling and heating cycles, potentially affecting printing conditions.18 Consequently, our experimental design adheres to a specific cooling cycle, accounting for the process of initially forming the cell suspension in a liquid state and subsequently allowing it to solidify at 4 °C. Thus, this study aimed to fabricate the tubular structure presented in Fig. 1(C).
To determine the optimal gelatin concentration for forming the inner layer of the structure, we analyzed the rheological properties of gelatin bioinks at concentrations of 1%, 2%, and 3% (w/v) and evaluated their response to temperature changes (Fig. 2(A)). Maintaining the gelatin bioink in an optimal gel state is crucial to ensure consistent ejection pressure while avoiding extremely low temperatures or high pressures that might damage the cells. A 2% gelatin concentration could maintain the gel state at 10 °C while ensuring stability at room temperature (20 °C). However, we selected a 3% gelatin concentration for its enhanced ability to manage the effects of cell density on printability and bioink properties.19,20
For the middle vascular layer of the intestine structure, collagen bioink was selected. This choice was grounded in two main reasons. Ensuring stable adhesion of the Caco-2 cells to the inner surface, and providing a stable environment for maintaining vascular cells. Uncrosslinked collagen bioinks are generally weak and unsuitable for 3D bioprinting without additional support materials. These bioinks solidify when exposed to temperatures above 37 °C, and it is typically recommended to crosslink them for at least 30 min to achieve optimal results. In this study, we explored whether partial crosslinking could improve the printability of collagen bioinks compared with the standard use of uncrosslinked collagen bioinks in the bioprinting process. To achieve this, the bioinks were exposed to a temperature of 37 °C for 15 min and then to 10 °C for an additional 60 min. The aim was to assess if these conditions could positively influence the printability of the collagen bioinks. Fig. 2(B) shows how the storage modulus, loss modulus, and the ratio of these values, tan(δ), change over time at different temperatures. A tan(δ) value greater than 1 indicates a liquid state, while a value closer to 0 indicates a solid state. From these observations, we determined that the best printing condition is when tan(δ) is in the range of 0.4–0.6, representing a scenario where the gelatin bioink in the central layer is supported by a thin, stable layer. Fig. 2(B) indicates that the collagen bioink, after being crosslinked at 37 °C for 15 min, achieves a stable tan(δ) value at 10 °C after approximately 10 min, suggesting that these conditions are effective for stable printing.
To establish the muscle layer that supports the structural integrity of the small intestine, a combination of alginate and collagen bioinks was used. Alginate bioinks are commonly used in coaxial nozzle printing techniques owing to their rapid and straightforward gelation when exposed to calcium chloride.21,22 Based on previous recommendations for optimal printing conditions, a combination of 4% (w/v) alginate bioink and 2% (w/v) calcium chloride was used as the crosslinker for the alginate–collagen bioink in this study.21 Furthermore, to mitigate the risk of cell death associated with high calcium chloride concentration or extended crosslinking duration,16 we established a crosslinking period for the 2% calcium chloride solution, ensuring it did not exceed 15 min. Given the acidic pH of calcium chloride solutions based on 1× PBS, which could be detrimental to the cells, DMEM was used as the solvent for calcium chloride preparation. Consequently, we opted to employ DMEM as the solvent for calcium chloride preparation.
While alginate and calcium chloride are commonly favored in coaxial 3D extrusion bioprinting owing to their convenient sol–gel transition properties,23 alginate is not conducive to long-term cell culture within 3D constructs due to its lack of cell-binding sites.24 To enhance cell viability and create a more faithful tissue mimic, we incorporated collagen bioink in conjunction with alginate bioink. The 4% alginate bioink was combined with 1% collagen bioink in a 1:1 ratio for effective formulation.
To demonstrate the consistent printability of the collagen-based bioinks (collagen bioink and collagen–alginate bioink) under specific conditions, we assessed their viscosity profiles at low melting points. The relationship between shear stress and shear rate was examined after crosslinking at 37 °C for 15 min and stabilization at 10 °C for 10 min, consistent with the conditions set before initiating the printing process (Fig. 2(C)). Both alginate–collagen bioink and collagen bioink exhibited pseudoplastic behavior, characterized by a decreasing rate of shear stress as shear rate increased. This behavior indicates that they are shear-thinning fluids, where viscosity diminishes as shear rate escalates. Such a rheological profile is highly desirable for extrusion-based bioprinting processes.
After confirming the printability of the bioinks, we evaluated their mechanical stability—a critical prerequisite for the safe and sustained cultivation of cells. Notably, increased stiffness and density do not necessarily yield superior outcomes, as excessive rigidity can negatively impact biological functions such as cell proliferation and differentiation, potentially resulting in unexpected cell behavior within the tissue.25,26 Additionally, it is essential to consider any changes in stiffness over the culture period, as rapid degradation of the material stiffness may lead to structural collapse and loss of support for the cells.27 As illustrated in Fig. 2(D), both the alginate and collagen bioinks exhibited a consistent storage modulus within an angular frequency range of 1–100 rad s−1, indicating that both bioinks retained their structural stability even after 12 h of incubation. The inclusion of collagen bioink did not compromise structural integrity, as evidenced by the stable storage modulus, which remained similar to that of the 4% alginate and 2% alginate scaffolds. Moreover, the collagen in the endothelial layer exhibited the necessary softness to facilitate the growth of endothelial cells, and the small pores did not hinder their capacity to form a vascular network (Fig. 2(D)).
Furthermore, Fig. 3(C) illustrates the bioprinted and fabricated tubular small intestine structure onto the chip platform, generating the final intestine-on-a-chip (IOC) model. We stained the Caco-2 within the tubular structures in the IOC using calcein AM and ethidium homodimer, as depicted in Fig. 3(D). Our findings demonstrated that epithelial cells actively proliferated and successfully adhered to the collagen endothelial layer. The significantly low number of dead cells observed by day 7 of culture strongly suggests that the gelatin bioink effectively shaped the hollow channel without inducing cytotoxicity.
The same experimental approach was employed for both endothelial cells and smooth muscle cells, with these cells integrated into the collagen and alginate–collagen layers, respectively. As illustrated in Fig. 3(D), both cell types exhibited robust growth in their designated layers, with no significant cell death observed. These results underscore the effectiveness of co-culturing smooth muscle cells, endothelial cells, and epithelial cells within the tubular structures, demonstrating that the system is capable of replicating the physiological environment of the small intestine and supporting normal cell functionality.
Lysozyme (LYZ) is an enzyme that plays a crucial role in the innate immune system, defending against bacterial infections.31 Within the villi, LYZ is primarily secreted at the crypts and plays a crucial role in protecting the epithelial cells. It is evenly distributed throughout both the mucus layer and crypts, ensuring comprehensive protection for the entire epithelial layer. Microvilli, situated on the apical side of the villi, serve to increase the surface area of the cell membrane, enhancing the functionality of the villi.32 The brush border, composed of numerous microvilli, is positioned closest to the intestinal lumen and plays a pivotal role in nutrient absorption. Villin-1 (VIL1), a cytoskeletal protein found in microvilli, contributes to structural support and amplifies the surface area for nutrient absorption (Fig. 4(D)). The results of villi height measurements across the different models (Fig. 4(C)) demonstrated a certain pattern pertaining to the effectiveness of villi formation that was consistent with the levels of LYZ and VIL1 staining observed in each model (Fig. 4(E)). Specifically, the staining intensities of both LYZ and VIL1 increased progressively from the dynamic transwell model to the static IOC model, and these values were the highest in the dynamic IOC model. These findings confirm that the dynamic IOC model not only supports the formation of well-structured villi but also replicates the key functionalities of crypts and villi most effectively. Therefore, the dynamic IOC model was validated as the superior platform for mimicking the structural and functional characteristics of the small intestine. The relative gene expression levels of LYZ and VIL1, determined through qRT-PCR, further supported these observations, showing that the dynamic conditions in the IOC model led to the tallest villi and most pronounced crypt formation (Fig. 4(F) and (G)).
We assessed the presence of MUC2 in both the transwell and IOC models to evaluate their ability for Mucin2 secretion. As shown in Fig. 5(A) and (B), dynamic transwell models exhibited limited MUC2 expression, whereas the IOC demonstrated more pronounced and positive MUC2 expression. Based on these findings, the presence of well-defined villi and crypts in the IOC model appears to significantly enhance MUC2 expression and secretion, indicating that cell interactions within the IOC structure play a key role in epithelial function. Additionally, previous studies support that the presence of endothelial cells, smooth muscle cells, and epithelial cells enhances epithelial functionality, suggesting a synergistic effect on the barrier integrity and immune responses of epithelial layers.35 Given that flow rates considerably affect the morphology of the intestinal barrier,36 it is essential to highlight the distinction in ZO-1 expression levels between the dynamic transwell model and static IOC. Despite the exposure to dynamic conditions in the transwell models, the static IOC exhibited superior ZO-1 expression levels, as illustrated in Fig. 5(A) and (C). These findings suggest that the formation of villi through the creation of a 3D tubular structure (Video S2†) is associated with improved barrier function in small intestinal in vitro models. In this context, the IOC cultured under dynamic conditions demonstrated the most favorable outcomes among the three models.
Fig. 5 Evaluation of MUC2 protein secretion of the mucus layer and ZO-1 for intestinal barrier integrity. (A) Immunostaining of MUC2 and ZO-1, with MUC2 detected in green and ZO-1 in red. Nuclei stained with DAPI (blue) (images were obtained from the same regions as in the schematic shown in Fig. 3., scale bar: 100 μm). Relative expressions of (B) MUC2 and (C) ZO-1, determined through qRT-PCR experiments. |
In the permeability test, a low molecular weight fluorescent dye with a molecular weight of 4 kDa was applied to the luminal side of IOC models. This molecular weight is adequately small to traverse the pericellular pathway, allowing for permeability experiments with more stringent criteria compared with the 40 kDa threshold, which just passes through the intercellular space. Fluorescent molecules rapidly passed through the porous membrane in the dynamic transwell model within only 5 min of treatment. In contrast, both the static and dynamic IOC models effectively prevented the passage of the fluorescent dye to the basolateral side, as illustrated in Fig. 6(C). To quantify permeability, we analyzed the intensity of the green fluorescence on the basolateral side across the three models using ImageJ software (Fig. 6(D)). This analysis revealed that the IOC models exhibited a lower level of fluorescence on the basolateral side compared with the dynamic transwell model, indicating better barrier function. These results confirm that the IOC models, cultured for 7 d, maintain robust intestinal barrier integrity, effectively preventing the passage of fluorescent molecules and demonstrating their capability to accurately replicate the intestinal barrier function.
Acetaminophen (APAP) is a commonly used over-the-counter analgesic and antipyretic.37 However, it has been reported to potentially harm the intestinal epithelium and pose a risk of liver toxicity.38,39 In light of these findings, we conducted drug metabolism tests using APAP concentrations of 5 mM, 10 mM, and 20 mM. Fig. 6(E) shows images depicting live and dead cells within the IOC. The number of dead cells within the IOC increased with rising concentrations of APAP. These observations suggest that the IOC effectively metabolized the drug, reinforcing its suitability as an intestinal in vitro model for drug delivery system studies.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4lc00731j |
This journal is © The Royal Society of Chemistry 2025 |