Open Access Article
Claudia
Olaizola-Rodrigo
ad,
Sujey
Palma-Florez
ef,
Teodora
Ranđelović
abc,
Clara
Bayona
ab,
Mehran
Ashrafi
a,
Josep
Samitier
cef,
Anna
Lagunas
ce,
Mònica
Mir
cef,
Manuel
Doblaré
abc,
Ignacio
Ochoa
*abc,
Rosa
Monge
*d and
Sara
Oliván
*ab
aTissue Microenvironment (TME), Lab. Aragón Institute of Engineering Research (I3A), University of Zaragoza, Zaragoza, Spain. E-mail: iochgar@unizar.es; soligar@unizar.es
bInstitute for Health Research Aragón (IIS Aragón), Zaragoza, Spain
cCIBER-BBN, ISCIII, Spain
dBEOnChip S.L., Zaragoza, Spain. E-mail: rmonge@beonchip.es
eNanobioengineering Group, Institute for Bioengineering of Catalonia (IBEC), Barcelona Institute of Science and Technology (BIST), Spain
fDepartment of Electronics and Biomedical Engineering, University of Barcelona, Martí i Franquès 1, 08028 Barcelona, Spain
First published on 6th March 2024
Organ-on-chip (OOC) technology has recently emerged as a powerful tool to mimic physiological or pathophysiological conditions through cell culture in microfluidic devices. One of its main goals is bypassing animal testing and encouraging more personalized medicine. The recent incorporation of hydrogels as 3D scaffolds into microfluidic devices has changed biomedical research since they provide a biomimetic extracellular matrix to recreate tissue architectures. However, this technology presents some drawbacks such as the necessity for physical structures as pillars to confine these hydrogels, as well as the difficulty in reaching different shapes and patterns to create convoluted gradients or more realistic biological structures. In addition, pillars can also interfere with the fluid flow, altering the local shear forces and, therefore, modifying the mechanical environment in the OOC model. In this work, we present a methodology based on a plasma surface treatment that allows building cell culture chambers with abutment-free patterns capable of producing precise shear stress distributions. Therefore, pillarless devices with arbitrary geometries are needed to obtain more versatile, reliable, and biomimetic experimental models. Through computational simulation studies, these shear stress changes are demonstrated in different designed and fabricated geometries. To prove the versatility of this new technique, a blood–brain barrier model has been recreated, achieving an uninterrupted endothelial barrier that emulates part of the neurovascular network of the brain. Finally, we developed a new technology that could avoid the limitations mentioned above, allowing the development of biomimetic OOC models with complex and adaptable geometries, with cell-to-cell contact if required, and where fluid flow and shear stress conditions could be controlled.
Microtechnologies permit the fabrication of cell culture chambers and provision and removal of nutrients and gases with micrometer precision, driving to the simulation of controlled biological environments where biological fluid continuously enters slowly but steadily, thus simulating the physiology of organs and tissues.5 These devices, known as OOC systems, allow mimicking tissue and organ functions, controlling physicochemical microenvironments and reproducing highly accurate tissue interfaces at a level that is not possible for 2D or 3D traditional culture systems. They also enable high-resolution real-time imaging and in vitro analysis of biochemical, genetic, and metabolic activities of living cells in a functional pseudo-organ context. This technology has enormous potential to produce disruptive advances in the study of tissue development, organ physiology, and disease etiology.4,6–8
Over the past years, engineered chemical gradients in OOC systems have attracted extensive attention in biomedical applications. Gradients play an essential role in many biological activities and regulate several cellular functions in vivo. These gradients of ions, oxygen, and proteins are constantly forming and dissipating within tissues.9–13 Gradients are also important in the physiological response to injury and diseases by immune cells.14–16 As a matter of fact, without these biological gradients, many cell functions could not be performed, and complex organisms would not develop. Moreover, chemical gradients affect diverse cellular behaviors such as migration, proliferation, differentiation, inflammation, or tumor evolution.17–21 For example, oxygen gradients are also related to cell growth, survival, and migration.22–24 Thus, producing controlled gradients in OOC systems is essential to obtain biomimetic environments and to evaluate those cellular processes in the OOC technology.25,26
Gradient devices made of different materials can be found in the literature, but most of the chips are based on micropillars27–31 to retain the hydrogel inside the chambers. However, these pillars create a physical barrier between the central chamber and the side channels, changing completely the gradient profile, especially close to the pillars. In addition, pillars also hinder direct cell-to-cell contact in co-culture models, which is relevant for some cell types, such as endothelia or epithelia, to the formation of tight junctions between cells to reach a functional barrier.32 Furthermore, cells can be retained in the pillars avoiding contact with other cells. Finally, pillars alter the shear stress distribution around them, which is especially critical in some applications, since it may change the cell behaviour of certain cell types, avoiding the possibility of getting realistic biomimetic models. To solve these drawbacks, some pillarless devices have been described in the literature. One of the technologies developed is the technique of parallel geometries. However, it was limited to parallel geometries where the shear stress is close to being uniform along the chip; this means that the limitation in terms of designs is high, as the geometries can only be created from three streams running in parallel.33–36 Another pillar free design is the phaseguide technology which consists of meniscus pinning barriers,37–39 but this technique does not allow the possibility of designing any geometry. Photopatternable hydrogels,40–43 although representing a cutting-edge technology, present a challenge due to the complex development and manipulation required, despite their capability to achieve highly varied designs and geometries.
In this work, we developed a microfabrication technique that allows the creation of different geometries and, thus, different shear stress distributions on the hydrogel boundary. This technology is based on a plasma surface treatment that is carried out with the geometry of the desired designs, as there is no limitation in terms of geometry.
To validate the biological feasibility of the chip, a blood–brain barrier model (BBB-on-a-chip) was developed. The BBB is a highly selective barrier that ensures the supply of oxygen and nutrients, avoiding the entry of pathogens or potentially harmful molecules and limiting the access of therapeutic molecules to the central nervous system (CNS).44 Due to the importance of achieving new therapies for central nervous diseases, the development of a functional BBB model is crucial. In this sense, the design of pillarless microdevices allows the formation of a continuous endothelium, in direct contact with human astrocytes and pericytes, thus helping the formation of the tight junctions (TJs) required for maintaining the restricted BBB permeability.
In summary, a new microfluidic fabrication process for pillarless thermoplastic chips is presented, as well as its validation in a relevant biological setting. This fabrication approach allows obtaining a wide range of geometries with variable and controlled shear stress distribution by creating a diffusion profile uninterrupted by the presence of pillars.
First, the microfluidic device was designed using two software codes: AutoCAD to design the 2D pattern and Solid Edge to establish the 3D model (Fig. 1A). Fig. S1† shows the SolidEdge views of the device. As mentioned above, the device consists of an injection molded part, with the channels defining the chip and the base. The pattern of the channels was done in 2D, and the channels of the final device were designed with the following dimensions: side channels of 0.8 mm in width, 3 mm wide and 4 mm long central chamber, and 1 mm central channel (Fig. 1A). The materials were cut using the 2D patterning process with a plotter (FC8600-60 Wide Vinyl Cutter, Graphtec), and the surface treatment was carried out, consisting of surface activation exposing the materials to oxygen plasma (0.4 mbar, 100 W (50%), 30 s), on the top and the base. For this purpose, an Atto plasma cleaner from Diener electronic was used. Finally, all the components were joined in two steps using a hot embosser (Digital Combo Heat Press, Geo Knight): firstly, the base was bonded to the channels, and then this assembly was bonded to the injection piece (Fig. 1D).
A magnifying lens (Nikon SMZ745) and a confocal microscope (Nikon Eclipse Ti) were used to check the measurements of the device to assess the reproducibility of the fabrication technique. For this purpose, the chamber width, the central channel width, and the height of the chamber were measured in 10 devices. Measurements of the mask and the final device were made with the magnifying lens after the cutting and fabrication processes. Three measurements were made in each area tested in each of the masks, that is, three in the central chamber and three in the central channel. The same process was performed for each of the final devices. The software used to make these measurements is Image Acquisition and Measurement Software IC Measure. Measurements of the seeded device were made by introducing a collagen hydrogel with fluorescent microspheres into the central chamber of the device and observing the chip under the confocal microscope. The same measurement process was used: 3 were made in each relevant area, the central channel width and the chamber width. On the other hand, the height of the channel was also measured, as fluorescence allows it. Nikon EZ-C1 FreeViewer and Fiji software were used for these measurements. Both the gel creation process and the seeding process are explained in the following section (Fig. 2).
To validate these geometries, a collagen gel (collagen type I, rat tail Corning, 354249) containing green FluoSpheres (FluoSpheres, Invitrogen, F8811) was introduced in the central chamber to observe its confinement and perfused with rhodamine (Rhodamine B, Sigma-Aldrich, R6626) in PBS through the side channels, as explained in section 2.3.
The fluid flow experiments were done using a syringe pump (NE-1000 Multi-PhaserTM) at 5 μL min−1 for 30 minutes. The syringes filled with 1 μg mL−1 Rhodamine B (Sigma-Aldrich, R6626) in PBS were connected to the chips using PTFE tubes (1/16′′ OD × 1/32′′ ID, Darwin Microfluidics) and screw connectors (1/4′′-28, Elveflow Microfluidics). The solution was perfused to test the confinement of the hydrogel and the diffusion process through the hydrogel.
To evaluate the hydrogel confinement inside the central chamber, the hydrogel distribution was assessed by confocal microscopy.
The corresponding CAD files were used to extract the geometries of the channels and chamber of each microdevice. In the channels, the Stokes equation was used to simulate the fluid flow under laminar conditions, while the fluid flow in the porous hydrogel that fills the chamber was modeled by means of the Darcy equation. These geometries were then meshed in Gmsh, an open-source finite element mesh generator.47 On average, around 330
000 elements with an average size of 0.1 mm were used for each device. The fluid was considered with water properties (density ρ = 1000 kg m−3, viscosity μ = 1 mPa s) and modeled as a monophasic and incompressible fluid under isothermal and laminar conditions, since the Reynolds number, Re = Lvρμ−1 is well below 100. A permeability of κ = 1.78 × 10−8 mm2 was considered for the hydrogel as a porous material.47 Boundary conditions for fluid flow were defined as a fixed flow of 10−5 kg s−1 at the inlets, atmospheric pressure (zero pressure) at the outlets, and zero velocity conditions along the channel walls. The oxygen diffusion coefficient throughout the device was considered D = 3.29 × 10−3 mm2 s−1.48 Boundary conditions for oxygen were considered fixed at the inlets, with a value of 0.21 × 10−9 mol mm−3, while the initial distribution of oxygen in all the domains was considered homogeneous with a value of 0.189 × 10−9 mol mm−3. Darcy–Stokes equations were solved in a steady state, while the mass transfer equation for oxygen was solved time-dependently. The velocity field obtained from the fluid flow in the channels and the chamber was used in the convection term of the oxygen transfer. The simulation time for mass transfer was 2 minutes as oxygen reaches steady state during this period based on the simulation conditions in this study and the changes after this time are negligible, aligning with the objectives of our study. All geometries were then analyzed under the same conditions, and the distributions of shear stress and oxygen concentration were computed as described in the Results and discussion section.
000 of each cell type was prepared and centrifuged at 1000g for 5 minutes. Meanwhile, a filtered solution of fibrinogen (3 mg mL−1 in PBS) (Sigma-Aldrich, F8630-16) and thrombin (100 UI in PBS) (Sigma-Aldrich, T4648) was maintained on ice. Then, the cell pellet was gently resuspended in 50 μL fibrinogen solution, and 1 μL of 125 mM CaCl2 (final concentration 2.5 mM) and 1 μL of thrombin (final concentration 2 UI) were added and rapidly mixed and injected gently into the central chamber. The chip was immediately flipped upwards and downwards every 20 seconds for 3 minutes to assure the homogeneous distribution of cells in the whole chamber height. Then, the chip was incubated for 25 minutes at 37 °C and 5% CO2 to promote hydrogel polymerization. After that time, the central chamber inlets were sealed with adhesive. Finally, the lateral fluidic channels were perfused with a mixture of astrocytes and ENDOGRO® medium in a ratio of 1
:
1 with all the supplements at the concentration needed for all cell types (BBB medium). Evaporation reservoirs were filled with PBS and the devices were maintained at 37 °C and 5% CO2. After 48 hours, the endothelial barrier assembly was performed in one of the lateral channels previously coated with a collagen solution (25 μg mL−1 in PBS) for 50 minutes to promote the cell attachment. Meanwhile, hCMEC/D3 cells were detached with 0.25% trypsin/EDTA (ThermoFisher Scientific, #25200056) and 150
000 cells were centrifuged at 1000g for 5 minutes and resuspended in 50 μL of BBB medium and immediately included in the collagen-coated channel. At this moment, the chip was left in a vertical position allowing the endothelial cells to make contact with the hydrogel wall by gravity for 2 hours at 37 °C and 5% CO2. The cell medium was changed every day until day 7, and bright-field microscopy images were taken on day 7 using an inverted optical microscope (Nikon Ti2 microscope).
Cell viability was also determined on day 7 using calcein-AM (ThermoFisher, C3100MP) to stain alive cells and ethidium homodimer-1 (EthD-1) (ThermoFisher, L3224B) for dead cells. A live/dead solution was prepared following the manufacturer's instructions, obtaining a solution with a final concentration of 2 μM calcein AM and 4 μM EthD-1 in PBS. The cells were incubated with the live/dead solution for 1 hour at room temperature and washed carefully with PBS twice. The cells in PBS were observed using an inverted fluorescence microscope (Olympus IX7).
:
100, ThermoFisher Scientific, 33-9100) and VE-cadherin (1 mg mL−1, 1
:
100, Abcam, ab33168) in 3% BSA in PBS-T were added and incubated overnight at 4 °C. Then, the cells were washed three times with PBS and incubated with fluorophore-conjugated secondary antibodies anti-rabbit Alexa 568 (2 mg mL−1, 1
:
1000, ThermoFisher Scientific, A-11036) and anti-mouse Alexa 488 (1
:
1000, ThermoFisher Scientific, A-10667) in 1% BSA in PBS-T for 2 hours at RT. Afterwards, the cells were incubated with Hoechst 33342 (1
:
1000, Invitrogen, H3570) for 15 min at RT. Finally, the cells were washed three times with PBS and the BBB was observed by confocal microscopy at 63× (Leica TCS SP5 Multi-photon system).
To validate this fabrication process, the reproducibility of the devices was studied. For that, measurements of the central channel were made throughout the manufacturing process using a magnifying lens and a confocal microscope. These measurements were taken on 10 devices from the same batch; thus, all fabrication processes were carried out on the same day. Firstly, the mask was measured, secondly the newly manufactured final device was measured, and finally the device seeded with collagen was measured. Regarding the central channel width, the measurements of the mask (1.04 ± 0.02 mm), the final device (0.98 ± 0.03 mm) and the seeded final device (1 ± 0.07 mm) were similar, and no significant differences were observed (Fig. 2). A similar result was obtained regarding the central chamber width; for the mask, the mean of the measurements was 3.11 ± 0.03 mm, for the final device, 2.94 ± 0.05 mm and for the seeded final device, 2.99 ± 0.13 mm (Fig. S3†). In relation to the height of the channels, the practical average was 196.56 ± 2.72 μm compared to the theoretical value of 200 μm, so no significant differences were noted (Fig. S3†). These results showed that the manufacturing process was carried out efficiently, and this methodology presents high reproducibility.
In this work, four different geometries that could be related to histological structures were fabricated. For example, it might be possible to simulate blood vessels under physiological or pathological conditions using the “guitar” and “diamond” patterns, which have similar shear stresses to capillaries and venules. Another example of close simulation is the intestinal villi, thanks to the “wave” design. In all cases, the same manufacturing process was used since there is no a priori limitation to obtain the desired geometry.
As with the original pattern, the confinement of the collagen gel into these devices was assessed. The results showed perfect confinement of the gel under static and flow conditions and diffusion over time for the proposed different designs (Fig. 3).
The distributions of fluid shear stresses and oxygen concentration obtained in finite element analysis using FEniCS are shown in Fig. 4 and 5. In Fig. 4, we examine the impact of pillars within the “gradient” chip on both shear stress distribution and oxygen concentration. The presence of pillars hinders fluid flow, resulting in reduced shear stress within the chamber. Conversely, in the abutment-free design, the channel–chamber interface exhibits higher shear stress and oxygen concentration. If we study all abutment-free models (Fig. 4 and 5), the shear stress along the channels was around 3.5 Pa, decreasing in regions close to the chamber. The “gradient” device shows the lowest shear stress in comparison with the other models. The geometry of this chip in inlets and outlets is different from the other models, and the boundary areas in this model are slightly greater than in the others. Also, the width of this model is bigger than the rest. All these differences in geometry cause the difference in shear stress, pressure drop, and velocity in this model compared to the others. The “hammer” and “gradient” devices were characterized by almost constant shear stress and velocity along the lateral channels (around 3.4 Pa and 2.6 Pa for shear stress and 70 mm s−1 and 120 mm s−1 for velocity, respectively). In these designs, without any section change in the channels, the value of the velocity and, consequently, the shear stress was constant along the channels.
![]() | ||
| Fig. 4 Computational simulation of the gradient designs: pillar-free and pillar-supported. (A) Shear stress profile in MPa. (B) Oxygen concentration along the device in mol mm−3. | ||
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| Fig. 5 Computational simulation of the devices of the designs guitar, waves and diamond. (A) Shear stress profiles in MPa. (B) Oxygen concentration in mol mm−3. | ||
Fig. S4† shows the velocity magnitude profile in a cross-section view of the devices. Like the shear stress, the velocity in the channel in the regions close to the chamber decreased compared to the velocity along the channels far from the chamber in all the models. Maximum velocity can be observed in the channels for all the models except for the “diamond”, which occurs in the regions close to the chamber and is about 160 mm s−1. In this model, at that region, the area of the channels is reduced and causes an increase in the velocity magnitude. In particular, the lowest velocity in the regions close to the chamber occurred in the “guitar” and “wave” shapes (approx. 65 mm s−1 and 60 mm s−1, respectively) (Fig. 5A). Concerning the “diamond” geometry, the velocity in the lateral channels was lower than in the other geometries (around 120 mm s−1), decreasing to 60 mm s−1 close to the chamber area. In the zone close to the central chamber, the velocity was lower in regions with wider areas and higher in the peaks (160 mm s−1 in the red area). In Fig. 4B and 5B, the oxygen concentration can be seen for the different designs. Oxygen diffuses and moves due to fluid flow convection. The simulation results show that it reaches a steady state quickly. As can be seen in these figures, the oxygen concentration is reduced in the chamber region due to the low fluid velocity in this region for all the designs.
In contrast, due to the ease of movement of fluid, there are substantial concentrations of oxygen in the channels. The maximum oxygen concentration is in the inlets, as can be expected, and is reduced along the channel. The “wave” design shows a better distribution of oxygen in the chamber in comparison with the other designs. Obviously, in all the designs, the oxygen concentration in the interface between channels and the chamber is higher than in the other regions of the chamber. For the pressure results (Fig. S4†), in all the geometries, the pressure drop between inlets and outlets was around 10−3 MPa.
The choice of the chip design depends on the purpose and goals of the research. Considerations such as ease and cost-effectiveness of fabrication, versatility for various applications, and the ability to mimic the in vivo environment of the cells and tissues under study, or to examine physiological or pathological processes, should be considered.52
The simulation results from this study indicate that the “gradient” design has the lowest shear stress distribution among the options, while the “diamond” design shows a higher amount of shear stress. If lower shear stress is required, as in the case of intestinal epithelial cells, the “gradient” design can be a suitable choice. Conversely, in situations where shear stress is important, such as for vascular endothelial cells to maintain the physiological function of blood vessels or metastatic cancer cells that move in tissues where higher shear stress is needed, the “diamond” design may be the better option.53
Clearly, the obtained computational simulation data provide relevant information about the shear stresses and behavior of the fluid inside the device. Therefore, computational simulation for the study of fluid dynamics in devices, together with the fact that tuneable hydrogel patterns can be generated, emerges as a powerful tool for OOC technology. Thus, by combining both tools, more biomimetic microdevices can be achieved, which allows going one step further in the development of more realistic in vitro models. Here, we have demonstrated that through this fabrication technique, we can achieve devices where cells can be subjected to different shear stresses along the channel as can happen in blood vessels or in the intestine.54–56 It also highlights the value computing the oxygen concentration at every point of the device which permits the oxygen gradients in the chamber to be controlled and optimized, as happens in different locations in the human body.
Under static conditions, the confocal microscopy images showed that the hydrogel maintained its shape and height over time (7 days), denoting the good confinement of the central chamber and high cell viability (Fig. S5†). A similar validation was performed under flow conditions. After seeding the devices with a collagen gel containing green FluoSpheres (central channel) and perfusing PBS with rhodamine (lateral channels), the hydrogel remained confined over time, and a process of diffusion through the gel was observed (Fig. 6). Here, the small size of rhodamine-B particles (10 μm) contributes to rapid diffusion within a short duration (as illustrated in Fig. 6, notable diffusion occurs every 5 minutes from 5 to 25 minutes).
The evidence presented has shown that the applied treatment allows confining the hydrogels within the central chamber (without pillars) over time and retaining them even under flow conditions. Coupled with this, diffusion with a continuous profile not disrupted by pillars has been observed inside the central chamber, generating gradients inside the device. Both parameters, diffusion and gradients, are critical in the development of 3D experimental models, so this device can be used to test the diffusion process or gradient formation related to the study of cellular metabolism (nutrients, oxygen…) or drug diffusion.
Finally, this device has been seeded with different hydrogels other than collagen, such as fibrin (shown below) and PLMA100 (data not shown). The result was the same: confinement of the hydrogel in the central chamber.
Meanwhile, a live/dead assay was performed to assess cell viability within the fabricated microdevice. The green signal from the endothelial cells indicated a nearly 100% survival rate until the seven-day period. Additionally, the hydrogel zone exhibited mostly viable cells. As a result, both the fibrin hydrogel and the fabricated microdevice demonstrated biocompatibility with neurovascular cultures such as human astrocytes, pericytes, and endothelial cells (Fig. 7D).
Finally, permeability assays were conducted using fluorescent tracers with different molecular weights. On day 7, NaFI (376 Da) and D70 (70
000 Da) were injected into the endothelial channel to evaluate the BBB's permeability performance (Fig. 7E) and fluorescence images were captured in the neuronal area. As Fig. 7E displays, the results obtained from the BBB-on-a-chip indicated size-dependent exclusion, where smaller molecules (NaFI: 3.90 ×10−5 cm s−1) passed through the BBB faster than larger ones (Dextran 70: 1.92 × 10−5 cm s−1). The permeability values obtained from our developed BBB were consistent with previous reports in the literature for microfabricated 3D models.58
In summary, an uninterrupted endothelial barrier was established which emulates the neurovascular network of the brain. Immunofluorescence images demonstrated the development of TJs between adjacent endothelial cells which are crucial for maintaining the restricted BBB permeability. Furthermore, permeability assays confirmed the ability of the assembled BBB to exclude molecules based on size, with permeability coefficient values consistent with those previously reported for microfabricated 3D models. Therefore, the results obtained confirm the potential of our pillarless microdevice for a functional 3D BBB model that could be used to evaluate potential therapies for CNS diseases.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3lc01082a |
| This journal is © The Royal Society of Chemistry 2024 |