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Figure 1 depicts the experimental setup, outlining the process of GelMA synthesis through a methacrylation reaction. The resulting product was then used to fabricate the hydrogel substrate, onto which ECs were seeded. Subsequently, the cells were introduced into the flow chamber for a 6 h flow experiment at 12 dyne/cm2.
1H NMR spectroscopy was used to assess the success of the methacrylation reaction (Figure 2A). The presence of a methyl group at 1.9 ppm and a vinylic peak between 5.4-5.6 ppm in GelMA confirmed successful methacrylation. Additionally, the decrease in the lysine peak at 3 ppm in GelMA indicates the consumption of lysine residues, which are replaced with methacrylate residues12,13,16. The stiffness of GelMA hydrogels was evaluated using a compression test, which showed that the compression moduli increased with GelMA concentrations (Figure 2B). Hydrogels composed of 4% and 8% (w/v) GelMA were used to mimic physiological (5 kPa) and pathological (10 kPa) matrix stiffnesses, respectively8.
The flow chamber was engineered to be cost-effective and for easy sterilization, by utilizing acrylic polymer that is UV-resistant. Its transparency facilitates real-time monitoring of hydrogels and flow conditions during experiments. Designed with three distinct layers, the chamber minimizes the risk of hydrogel damage during loading or unloading: the bottom plate provides a sturdy base, the middle layer offers lateral support for the hydrogels, and the top plate, along the gasket, creates the clearance necessary for fluid flow (Figure 3A). Computational simulations were conducted using CFD to assess flow conditions and shear stress within the chamber. The following equation - shear stress = 0.0558 x flow rate - calculated the applied shear stress to the cells based on the flow rate as an input (Figure 3B). Notably, changes in material properties, such as stiffness, did not alter shear stress in the simulations. To count for differences in the hydrogel size in the final experimental setup, the hydrogels were intentionally sized slightly smaller in the computational model. A 0.5 mm gap was created between one side of the hydrogels and the chamber's middle plate walls, perpendicular to the flow direction. This configuration allowed for the analysis of shear stress effects in these gaps. While irregularities in shear stress were observed at gap locations (Figure 3B), their impact was confined to a small area adjacent to gaps, with the remaining hydrogel surface experiencing uniform shear stress (Figure 3C). These insights suggest discarding cells from the edges of hydrogels to minimize the potential impact of turbulent regions. It is worth mentioning that higher shear stress, up to 15 dyne/cm², was experimentally applied to ECs seeded on 5 kPa and 10 kPa hydrogels with no leakage in the device (data not included). However, increasing shear stress further could potentially result in cell detachment and hydrogel failure, emphasizing the need for careful optimization of experimental conditions.
For seeding cells to form a monolayer, it is crucial to use a higher cell density than in traditional cultures. Low seeding density has been shown to hinder the monolayer formation on softer hydrogels8. Additionally, pre-coating hydrogels with gelatin before cell seeding enhances initial cell attachment and spreading on softer hydrogels. However, it is important to note that the beneficial effect of this coating is temporary, as it primarily facilitates the initial interaction between the cells and the substrate.
Figure 4 demonstrates how stiffness and shear stress influence the formation of actin fibers. Under shear stress, thicker stress fibers formed, suggesting a stronger attachment to the surface. In softer samples, there were more peripheral actin fibers, which are indicators of physiological conditions. However, in ECs on stiffer substrates, the presence of stronger stress fibers and fewer peripheral fibers could potentially lead to EC dysfunction17. This data confirms the effectiveness of the presented system in modulating EC behavior.

Figure 1: Overview of the current study. (A) GelMA synthesis. Gelatin was chemically modified to gelatin methacrylate (GelMA) through a reaction between gelatin and methacrylic anhydride (MAH) at 55 °C. The product was then precipitated in acetone and dried under a vacuum. (B) Hydrogel fabrication. The cover glass was prepared by attaching spacers. Then, the modified glass was attached to the cover glass. The cover glass was placed on the mold, with the spacers providing the desired clearance between the modified glass and the bottom of the mold. The GelMA solution containing initiators was added to the opening between the modified glass and the mold, polymerizing to form a hydrogel covalently bound to the modified glass. (C) Flow experiment. The resulting hydrogel was used to seed ECs. After forming a monolayer, the cells underwent a 6 h flow experiment at a shear stress of 12 dyne/cm². This figure was created with BioRender.com. Please click here to view a larger version of this figure.

Figure 2: 1H-NMR spectra for gelatin and GelMA pre-polymerization. (A) Refer to dashed-lined boxes for relevant peaks. Methacryloyl peaks (i.e., vinylic and methyl groups) appeared after the chemical modification of gelatin, while the lysine group was used to quantify the degree of substitution following the chemical reaction18. (B) Young's modulus of the hydrogels was measured by a compression test, and 4% (w/v) GelMA hydrogels were considered as physiological substrates, and 10% (w/v) was considered as pathological substrate (n=4, mean ± SEM). This figure has been modified from8. Please click here to view a larger version of this figure.

Figure 3: Parallel-plates flow chamber design and computational simulation. (A) Three separate plates were used to reduce the possibility of damaging the hydrogels during loading or unloading; where the bottom plate provided a backing surface, the middle surface offered lateral support for the hydrogels, and the top plate and gasket formed the clearance for the fluid to flow. (B) The flow chamber underwent computational simulations11. When the flow rate is 215 mL/min, the shear stress along the drawn line is approximately 12 dyne/cm2, representing the physiological shear stress. (C) The influence of the 0.5 mm gap is confined to a small area adjacent to the gap. The remaining surface of the hydrogel experiences uniform shear stress. Please click here to view a larger version of this figure.

Figure 4: Shear stress and stiff hydrogel increase stress fiber formation. More peripheral actin fibers are formed in ECs on 5 kPa samples under flow. Stronger stress fibers were formed when the cells were exposed to shear stress on 10 kPa hydrogels, showcasing the model's effectiveness on EC's behavior. Arrows indicate peripheral actin, and the asterisks indicate stressed fibers. Scale bar= 10 µm (Blue: DAPI, Red: Actin Fibers). Please click here to view a larger version of this figure.