Microfluidic scaffolds for tissue engineering
Nak Won Choi, Mario Cabodi, Brittany Held, Jason P. Gleghorn, Lawrence J. Bonassar & Abraham D. Stroock
Nature Materials 6, 908 - 915 (2007)
Summary:
This paper proposes a method to control the microenvironment of cultured cells in 3-dimensions. Choi et al achieve this by creating microfluidic networks inside of a cell-seeded hydrogel to help distribute desired chemicals throughout the scaffold. This system allows for temporal and micrometer-scale spatial control of the biochemical environment. In simple terms, this tissue scaffold is a cell-seeded biomaterial made to have a network of small channels running through it, allowing for solutions to flow through by some external pressure force. Solute exchange may then occur by convective mass transfer between the flowing solution and the microchannel wall, and by diffusion from the channel walls through the rest of the gel.
To ensure efficient transport of solute through the channels and hydrogel, the scaffold must be suitable for different types of solutes. Here, they are categorized as: reactive (e.g. metabolites and waste) and non-reactive (e.g. signaling molecules and buffers). For reactive solutes, variations in solute concentration should be minimized; this is accomplished by setting a maximum spacing between channels (Figure 1a). This distance is determined using a characteristic diffusion-reaction variable (Krogh length). For non-reactive solutes, channels in the forms of sources and sinks are necessary for controlled gradients at steady state (Figure 1b).
A 3D scaffold made of calcium alginate containing microfluidic structures is populated with different cell types. The fabrication of the microfluidic scaffold is shown in Fig 2 and detailed in the Methods and Supplementary sections; in short, soft lithography of silicone creates a mould to create microchannels in the hydrogel, which is then cross-linked to aluminum jigs.
[proof of concept]
In 3D cell cultures, diffusion of both small and large molecules must be unobstructed. Here, diffusivity is measured by injecting a fluorescent dye comprised of both small and large fluorescent-labeled molecules into the microfluidic scaffold. The solute distributes throughout the gel by pure diffusion; the amount of fluorescence is quantified along with time and distance diffused. Diffusivity of both large and small solutes is said to be constant since fickian diffusion and exponential decay is observed. This result leads the group to conclude that diffusion of different sized molecules is unhindered within the pores of the gel.
Besides transport within the gel (diffusion), there is also a flow of solutions through the scaffold (convective mass transfer). To optimize the system, flow speed needs to be high enough so that the concentration of solute remains constant (i.e. equal to the inlet concentration) through the length of the channel; this ensures that the overall mass transfer process is diffusion-limited, and dependent on a controllable variable—the inlet concentration.
Choi et al. also demonstrate the ability to change out the solutes in the scaffold such that solute concentration is uniform across the microfluidic network. Figure 3f shows fluorescent micrographs of the scaffold at different time points after sequential delivery of green (fluorescein) and red (rhodamine) solutes to the scaffold. The dyes are observed to fill the microchannels and then spread out to cover the scaffold uniformly.
[other operational considerations]
A microfluidic scaffold also allows control of the metabolic environment of the cell culture. Choi et al. opt to obtain a uniform distribution of reactive solutes (e.g. metabolites and toxic waste products) across the length of the scaffold. To this end, they try to find the maximum separation between microchannels that satisfies the above criteria. Their experiment involves the metabolite calcein-AM, which forms a fluorescent product when taken up by the cell. The metabolites are delivered via a microfluidic network with variable spacing between channels (Fig 4b). The result proved the possibility of a uniform metabolic environment, and that scaffold geometry is an important factor to consider.
More than one independent microfluidic network may be used to allow steady-state gradients in the solute concentrations (Fig 5). This would prove useful and convenient in studying cellular response to different concentrations of solute.
Comments:
Overall, the paper does a good job of proving the viability of the microfluidic scaffold in providing a means of controlling the biochemical environment. A wide range of solute sizes is proven to be effectively exchanged with the scaffold. Also this concept has useful applications including: growing thick tissue; providing a means of inducing certain cell development; and providing a basis for bioreactors.
It seems that this approach could be time-consuming and difficult to create for different combinations cell types and biomaterials. It would be interesting to see how many of these combinations are useable with the microfluidic scaffold approach, and if this is a limiting factor in experimentation. Also, since cell cultures tend to be affected by fluid shear forces, the microfluidic scaffold approach may induce some unwanted differentiation in the cells close to the microchannels.
7 comments:
Do they ever address the diffusion of small solutes through the (presumably) PDMS of the device itself?
The biomaterial used was calcium alginate hydrogels. They claim that it has high diffusive permeability to small (and large) molecules; a number of studies are referenced as proof.
It is noted that 3D cell cultures are important for culturing specific types of cells. Do you know how one would remove cellular debris and waste in a microfluidic scaffold? Would it be dependent on diffusion?
Just curious, what types of cells were seeded into the hydrogel?
There is mention that to optimize the system, the flow speed needs to be high enough to maintain a constant solute concentration. How is the fluid speed controlled? Is it manually flushed into the system or done with a syringe pump of some sort? You mentioned the possibility of shear forces due to fluid flow causing changes in cell behavior - do you think this is a significant issue and how does its importance compare to maintaining a high enough speed to keep a constant concentration?
Regarding the fabrication of the device, I'm assuming cells were seeded before the alginate was gelled. Does this affect the cells and did they do a study of gel kinetics to ensure appropriate gelling time to prevent cellular clumping?
You mentioned that non-reactive solutes require Sinks. It seems apparent that these sinks are other channels in the gel that are perfused with media without solutes. Looking at Figure 4a, I couldn't figure out where they placed the waste channels. Does the paper specify a specific placement? Are these waste channels parallel to the other channels or are they oriented perpendicularly in the black space in Figure 4a?
Johnny,
Yes, it should be diffusion limited. Waste should diffuse from the cell to the microchannels, where convective transfer should carry the waste away.
Michelle,
L2 (rat lung epithelial) cells and HepG2/C3A (human hepatocytes) cells and primary bovine chondrocytes were tested.
They do not report what they used to generate external pressure-driven flows; but I imagine that it is not manually driven.
I don't expect the shear effect due to fluid flow to be significant enough to make this system unusable; however, it might be something to consider when testing for something that may be influenced by shear forces.
Nikki:
They evaluated cell viability after stirring and injecting the seeded gel; viabilities were reported to be high.
Regarding your second question--calcium alginate hydrogels have already been used and characterized for cell seeding.
Philip:
I mentioned that sinks were necessary if controlled gradients were desired. However, the purpose of the Fig.4 experiment was to create a uniform steady-state distribution.
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