Umut Can Coskun1, Funda Kus2, Ateeq Ur Rehman3, Berna Morova4, Merve Gulle5, Hatice Baser2, Demet Kul6, Alper Kiraz4,7, Kemal Baysal6,8, Ahmet Erten5. 1. Faculty of Aeronautics and Astronautics, Istanbul Technical University, Istanbul 34469, Turkey. 2. Department of Biomedical Sciences and Engineering, Koç University, Istanbul 34450, Turkey. 3. Biomedical Eng. Technology Program, Foundation University Islamabad, Islamabad Phase-I, DHA, Pakistan. 4. Department of Physics, Koç University, Istanbul 34450, Turkey. 5. Department of Electronics and Communication Engineering, Istanbul Technical University, Istanbul 34469, Turkey. 6. School of Medicine, Department of Biochemistry, Koç University, Istanbul 34450, Turkey. 7. Department of Electrical and Electronics Engineering, Koç University, Istanbul 34450, Turkey. 8. KUTTAM, Research Center for Translational Medicine, Koç University, Istanbul 34450, Turkey.
Abstract
Compared to the established monolayer approach of two-dimensional cell cultures, three-dimensional (3D) cultures more closely resemble in vivo models; that is, the cells interact and form clusters mimicking their organization in native tissue. Therefore, the cellular microenvironment of these 3D cultures proves to be more clinically relevant. In this study, we present a novel easy-to-fabricate microfluidic shallow trench induced 3D cell culturing and imaging (STICI3D) platform, suitable for rapid fabrication as well as mass manufacturing. Our design consists of a shallow trench, within which various hydrogels can be formed in situ via capillary action, between and fully in contact with two side channels that allow cell seeding and media replenishment, as well as forming concentration gradients of various molecules. Compared to a micropillar-based burst valve design, which requires sophisticated microfabrication facilities, our capillary-based STICI3D can be fabricated using molds prepared with simple adhesive tapes and razors alone. The simple design supports the easy applicability of mass-production methods such as hot embossing and injection molding as well. To optimize the STICI3D design, we investigated the effect of individual design parameters such as corner radii, trench height, and surface wettability under various inlet pressures on the confinement of a hydrogel solution within the shallow trench using Computational Fluid Dynamics simulations supported with experimental validation. We identified ideal design values that improved the robustness of hydrogel confinement and reduced the effect of end-user dependent factors such as hydrogel solution loading pressure. Finally, we demonstrated cultures of human mesenchymal stem cells and human umbilical cord endothelial cells in the STICI3D to show that it supports 3D cell cultures and enables precise control of cellular microenvironment and real-time microscopic imaging. The easy-to-fabricate and highly adaptable nature of the STICI3D platform makes it suitable for researchers interested in fabricating custom polydimethylsiloxane devices as well as those who are in need of ready-to-use plastic platforms. As such, STICI3Ds can be used in imaging cell-cell interactions, angiogenesis, semiquantitative analysis of drug response in cells, and measurement of transport through cell sheet barriers.
Compared to the established monolayer approach of two-dimensional cell cultures, three-dimensional (3D) cultures more closely resemble in vivo models; that is, the cells interact and form clusters mimicking their organization in native tissue. Therefore, the cellular microenvironment of these 3D cultures proves to be more clinically relevant. In this study, we present a novel easy-to-fabricate microfluidic shallow trench induced 3D cell culturing and imaging (STICI3D) platform, suitable for rapid fabrication as well as mass manufacturing. Our design consists of a shallow trench, within which various hydrogels can be formed in situ via capillary action, between and fully in contact with two side channels that allow cell seeding and media replenishment, as well as forming concentration gradients of various molecules. Compared to a micropillar-based burst valve design, which requires sophisticated microfabrication facilities, our capillary-based STICI3D can be fabricated using molds prepared with simple adhesive tapes and razors alone. The simple design supports the easy applicability of mass-production methods such as hot embossing and injection molding as well. To optimize the STICI3D design, we investigated the effect of individual design parameters such as corner radii, trench height, and surface wettability under various inlet pressures on the confinement of a hydrogel solution within the shallow trench using Computational Fluid Dynamics simulations supported with experimental validation. We identified ideal design values that improved the robustness of hydrogel confinement and reduced the effect of end-user dependent factors such as hydrogel solution loading pressure. Finally, we demonstrated cultures of human mesenchymal stem cells and human umbilical cord endothelial cells in the STICI3D to show that it supports 3D cell cultures and enables precise control of cellular microenvironment and real-time microscopic imaging. The easy-to-fabricate and highly adaptable nature of the STICI3D platform makes it suitable for researchers interested in fabricating custom polydimethylsiloxane devices as well as those who are in need of ready-to-use plastic platforms. As such, STICI3Ds can be used in imaging cell-cell interactions, angiogenesis, semiquantitative analysis of drug response in cells, and measurement of transport through cell sheet barriers.
In
diverse fields such as basic research, drug development, and
regenerative medicine, the established experimental approach to study
cells is culturing them on a surface. This monolayer culture approach,
in which cells are maintained on polystyrene surfaces in cell culture
flasks, is termed two-dimensional (2D) culture. Although established
and straightforward, these systems allow for cell–cell interactions
only in 2D and do not recapitulate the complex cellular interactions
found in native tissues.[1]Growing
cells in three-dimensional (3D) structures more closely
resembles their existence in vivo; that is, the cells interact and
form clusters mimicking their organization in native tissue. This
3D organization has been shown to support the maintenance of the correct
phenotype of cells. Therefore, the cellular microenvironments of these
3D cultures are more clinically relevant.[2] In addition, 3D systems allow the experiments to be scaled down
to a microscale, thus reducing the number of cells and volume of chemicals
required.[3] These 3D approaches play a vital
role in filling the knowledge gap between 2D cell culture methods
and in vivo animal experiments.[4,5] Hence, there is a growing
necessity for the development of in vitro platforms mimicking the
physiological in vivo systems through the formation of highly structured
3D microenvironments that are reproducible and cost-effective as well
as accessible for imaging with microscopy. To this aim, microfluidic
platforms have led to the development of new testing methodologies
for conducting in vitro studies.Microfluidic platforms enable
precise manipulation of microenvironments
and high-resolution real-time monitoring of cells and small volumes
of liquids in microchannel networks in 3D.[6] In order to control and monitor the environment of 3D microculture
systems, various hydrogels that can be formed in situ within the microchannels
are used to support cell adhesion and growth.[7] These hydrogels can be natural polymers (collagen, fibrin, gelatin)
as well as synthetic polymers consisting of biocompatible monomers
such as poly(ethylene glycol) (PEG) and poly(lactic-co-glycolic acid) (PLGA).[8] Placing cells
and spheroids inside or on the surface of the hydrogels in microfluidic
platforms enables one to culture and optically image them in 3D for
extended periods of time. Such microfluidic platforms have enabled
researchers to monitor tumor angiogenesis[9,10] and
tumor extravasation[11−13] in greater detail and accuracy. Furthermore, 3D-functional
and perfusable microvascular networks composed of human endothelial
cells and bone marrow-mesenchymal stem cells (BM-hMSCs) have been
formed using microfluidic platforms.[14]Although the materials and methods used for the fabrication of
microfluidic cell culture platforms vary, soft lithographical fabrication
with polydimethylsiloxane (PDMS) is the most common, since it allows
for rapid prototyping. PDMS-based cell culture platforms also benefit
from the advantageous material properties of PDMS; that is, PDMS is
optically transparent, gas permeable, and can be easily bonded to
other transparent materials such as glass.[15,16] Earlier PDMS platforms have included integrated posts, commonly
referred to as “micropillars”, between channels to ensure
the confinement and support the stability of hydrogels.[13,17,18] In such a design, there exist
two or more microchannels all having individual inlets and outlets
that are isolated from each other with a middle channel, where a hydrogel
such as collagen is confined and mechanically supported by micropillars
placed in certain shapes and separations acting as burst valves. After
cells are seeded and cultured on the hydrogel, various molecules and
chemicals can be added to the adjacent side channels. The communication
between the side channels is limited to diffusion and convection through
the hydrogel formed within the middle channel acting as a porous medium.
The concentration, pressure gradients, and surface tension in such
a platform can be controlled to stimulate the cells in real time from
the side channels.[19] The response of cells
to these stimulations such as cell proliferation, migration into the
gel, angiogenesis, vasculogenesis, metastasis, and spheroid growth
can be monitored using a confocal microscope with high resolution
and in real-time.[20−23] However, micropillar-based 3D cell culture platforms have two major
limitations. First, the surface area where chemicals can be exchanged
between the central hydrogel and side channels is limited by the need
for frequent placement of micropillars.[20] Second, parameters such as the distance between the micropillars
and the design of a micropillar’s cross-section have drastic
effects on the confinement of hydrogel within the middle channel and
require sophisticated microfabrication facilities. This complex design
may also limit the adoption of materials besides PMDS and the applicability
of mass manufacturing methods such as injection molding and hot embossing.To overcome these limitations, various approaches have been reported
in recent years. Lam et al.[24] demonstrated
liquid confinement using a surface-tension-based liquid guide in a
microfluidic channel by printing a hydrophilic path on hydrophobic
substrates and vice versa. They reported that the confinement of liquid
along the printed guides depends on the aspect ratio of a liquid cross-section
and the surface wettability. They confined the liquid on the guide
via a sudden change in the surface contact angle. Similar to the work
of Lam et al.,[24] Lee et al.[25] confined the liquid along multiple guides due
to the sudden change in the capillary force by means of a sudden expansion
in the channel geometry. They also demonstrated the effects of height
and the width of the confined liquid on the success rate of the liquid
confinement along their guides. Hwang et al.[26] proposed a rapid prototyping method for a PDMS-based microfluidic
device, where confinement of liquid is achieved by capillary action
by using multilayered adhesive tapes for mold production. Tung et
al.[27] also developed a microfluidic platform
with a collagen hydrogel residing in a central channel. They confined
the hydrogel solution using 5 × 10 μm cross-sectioned ridges,
which increase the difference between advancing and receding contact
angles to provide guidance. Lee et al.[28] describe an injection-molded plastic array 3D culture platform (IMPACT),
a circular-shaped well array with capillary guided hydrogel loading.
The top surface of this circular platform is divided into two halves
by a rail and open for easy access. A collagen solution is loaded
from either half, confined around the corners and in the rail by capillary
action. Although this design makes the hydrogel more accessible and
is simpler than using micropillars, real-time control of chemical
gradients and pressure in the cartridge is much harder. Another limitation
of this system is the requirement of larger liquid volumes in the
side channels (several hundred microliters) in comparison to 10–20
μL in typical polydimethylsiloxane microfluidic platforms.[18,29]In our study, we present a novel, easy-to-fabricate, microfluidic
shallow trench induced three-dimensional cell culturing and imaging
(STICI3D) platform, suitable for both rapid-fabrication and mass-manufacturing
methods. STICI3D has a simple geometry for 3D cell cultures inside
or on the surface of a hydrogel confined within a shallow trench fully
in contact with two side channels for precise real-time control of
a cell microenvironment such as chemical gradients and pressure. In
our design, by achieving hydrogel confinement without necessitating
micropillar-based burst valves, we significantly simplified the device
design and maximized the surface area through which the hydrogel exchanges
media with the side channels. The capillary-based STICI3D design allows
it to be fabricated with soft lithography using molds prepared with
adhesive tapes and razors alone, which supports the easy adoption
of materials and methods for mass production such as hot embossing
and injection molding as well. Moreover, STICI3D requires only small
volumes of hydrogel (∼3 μL) or chemicals.To streamline
the STICI3D design and development, a meticulous
investigation of the effect of design parameters on the confinement
of hydrogel solution within the shallow trench was achieved with Computational
Fluid Dynamics (CFD) simulations, which allow for a numerical evaluation
of microfluidic cell culture system designs along with their respective
flow rates and patterns prior to fabrication.[30] In this study, we employed a numerical setup compatible with similar
flow problems reported in the literature and our previous studies.[31,32] We investigated the effects of individual design parameters such
as corner radii, channel height, and selection of surfaces with different
wettability under various loading pressures on the confinement of
a hydrogel solution within the shallow trench numerically using CFD
simulations supported with experimental validation. To assay the compatibility
of STICI3D with cell culture, we examined the attachment and proliferation
of human mesenchymal stem cells in the central collagen channel. Finally,
we also demonstrated that human umbilical cord endothelial cells (HUVEC)
lining the collagen respond to the molecules diffusing through the
hydrogel.This article is organized as follows. In the following
section,
after the STICI3D design is introduced, the CFD-based numerical model
and experimental setup is explained. In the order of presence; verification
and validation of the numerical method and results of numerically
and experimentally investigated design parameters on the confinement
of liquid within the shallow trench are presented in the subsections,
followed by the experimental results of exemplary 3D cell cultures.
Finally, conclusions are discussed in the final section.
Materials and
Methods
Design of STICI3D Platform
The proposed simple design
of the STICI3D platform consists of two side channels (shown in blue
in Figure a) and one
shallow trench in the middle (shown in red in Figure a), each having individual inlets and outlets.
The inlet and outlet chambers for the shallow trench were designed
to be 4 mm in diameter and the same height (h) as
the trench in order to reduce the confinement problems during the
hydrogel loading. To further reduce the end-user dependent variations
in loading the hydrogel solution, the diameter of the inlet for the
shallow trench was designed to be larger than the diameter of the
pipet tip to keep the liquid loading pressure close to atmospheric
pressure. The inlet diameter of the trench in STICI3D was reduced
when a higher inlet pressure was required for experimental testings
of the parameters (The 2D sketch of the design can be seen in Figure S1).
Figure 1
(a) 3D geometry of STICI3D, (b) half cross-section
view of the
STICI3D at the midsection, and (c) detailed view of the cross-section
at trench to the side channel joint.
(a) 3D geometry of STICI3D, (b) half cross-section
view of the
STICI3D at the midsection, and (c) detailed view of the cross-section
at trench to the side channel joint.The geometry of the STICI3D platform is one continuous chamber
with the height “h” of the shallow
trench (shown in red in Figure a) being shorter than the height “H” of the adjacent side sections shown in blue. Figure b shows the half cross-section
of the STICI3D microfluidic platform at midplane highlighted in Figure a. The detailed view
of this cross-section at the vicinity of trench to the side channel
joint, marked as detail B, is shown in Figure c. The geometry of the test section of the
STICI3D is constrained to have a constant cross-section as shown in Figure c.In order
to identify the range of STICI3D design parameters for
a successful confinement of the liquid within the trench, design parameters
such as the height of the trench h, selection of
hydrophilic surfaces, the contact angle of the hydrophilic surfaces,
and radii r at the corners of the trench were investigated
both numerically and experimentally where possible. An experimental
investigation of some design parameters was impractical due to difficulties
such as obtaining the desired surface contact angles. Therefore, for
those impractical cases the prediction of liquid confinement was limited
to CFD simulations only. To identify safer design values against the
overflow of liquid into side channels, which might result from possible
manufacturing or end-user dependent failures, STICI3D designs that
successfully confined the liquid at 0 Pa loading pressure were also
investigated numerically using higher loading pressures, and these
designs were validated experimentally where possible.
Numerical Setup
A finite volume-based commercial software
Ansys Fluent was used as the flow solver to investigate the two-phase
flow of immiscible fluids. The simulations were designed as two-phase,
transient, incompressible, 2D, and laminar. The volume of fluid method[33] (VOF) was used to track the interface between
two immiscible fluids, namely, air and liquid, where the Continuum
Surface Stress method with wall adhesion was chosen to model the surface
tension and adhesion.Collagen Type I was selected as the hydrogel
to be tested in our STICI3D design studies. The contact angles of
deionized water and hydrogel solution on the surface of PDMS, plain
glass, and poly-d-lysine (PDL)-coated glass (PDLcG) in a
medium of air were experimentally obtained at the early phases of
the study (see Section 1.4 in the Supporting Information). Since the difference in contact angles of water and hydrogel solution
were less than 10° for all of these surfaces, water and hydrogel
solution were assumed to have similar wetting behavior for the tested
material surfaces. Considering that deionized water is cheaper than
collagen, most of the experiments in the STICI3D design study and,
therefore, numerical studies were conducted with deionized water as
the liquid phase. In all simulations, the liquid is modeled as Newtonian,
where its density and viscosity were selected constant and the same
as those of water.Even though the problem had a steady nature,
since there was no
distinct and steady inflow, the simulations were conducted as transient.
An explicit VOF formulation with a sharp interface modeling was chosen
for high accuracy. Second-order upwind and geo-construct spatial discretization
schemes were again preferred to have high accuracy for the momentum
and volume fraction, respectively. The downside of the explicit formulation
was that it had a Courant-based time step size constraint. A dynamic
adaptive mesh refinement and variable time-stepping methods were employed
to reduce the required number of cells to a minimum and to keep the
maximum Courant Number lower than 0.25, which yields a varying time
step size in the order of 10–8 s as a result of
the adapted mesh sizes in most of the cases of this study.
Computational
Mesh, Boundary Conditions, and Solver Settings
A full 3D
representation of the problem in CFD calculations was
first attempted; however, this approach was found to be impractical
due to high computational costs. Extremely fine mesh sizes were required
in the vicinity of the air–liquid interface, which also forces
the time step size to be very small. The resulting 3D computational
mesh was predicted to have 100 million cells and was expected to run
for at least 105 time steps for each case. However, the
length of the trench is 2 orders of magnitude larger than its height
(see Figure S1 in the Supporting Information),
where the liquid is assumed to take the shape of this area and be
confined, suggesting that a 2D representation is valid for a variety
of parametric numerical investigations. Therefore, instead of modeling
the flow inside the whole STICI3D in 3D, a cross-section of the fluid
volume in the middle of the channel highlighted in purple in Figure a was selected as
the computational domain. Given the symmetrical nature of the problem,
half of the cross section was taken as the computational domain to
further reduce the computational costs. Both the 3D fluid volume and
the chosen 2D computational domain are shown in Figure a.
Figure 2
(a) 3D volume of fluid inside the STICI3D and
2D computational
domain chosen to investigate confinement of liquid within the trench
shown in red, (b) 3D profile of hydrogel colored with Rhodamine B,
imaged with a confocal microscope using a z-stack function, (c) 2D
computational domain, initial and boundary conditions. Red and blue
areas represent liquid and air phases, respectively. Faces with symmetry,
pressure inlet, and pressure outlet boundary types are highlighted
in yellow, green, and pink, respectively. All boundaries that are
not highlighted are treated as a wall with no-slip boundary condition.
(a) 3D volume of fluid inside the STICI3D and
2D computational
domain chosen to investigate confinement of liquid within the trench
shown in red, (b) 3D profile of hydrogel colored with Rhodamine B,
imaged with a confocal microscope using a z-stack function, (c) 2D
computational domain, initial and boundary conditions. Red and blue
areas represent liquid and air phases, respectively. Faces with symmetry,
pressure inlet, and pressure outlet boundary types are highlighted
in yellow, green, and pink, respectively. All boundaries that are
not highlighted are treated as a wall with no-slip boundary condition.In this two-phase flow problem, air is selected
as the carrying
fluid, and water is selected as secondary. Since the main concern
of the simulation is to predict the final shape of the interface and
the condition of the confinement of the liquid within the shallow
trench, the volume fraction of water within the trench is initialized
as 1 in all cases, which indicates the trench is initially filled
with liquid. The inlet and outlet sections of the actual 3D channel
are out of the selected 2D computational domain. However, in order
to model this flow problem in 2D, the required inlet and outlet boundaries
were placed sufficiently away from the air–water interface.
The details of the 2D computational domain, as well as the initial
and boundary conditions of the flow problem, are shown in Figure c. The inlet of water
and outlet of air were highlighted in green and pink, respectively.
The left vertical boundary highlighted in yellow was selected as a
symmetry boundary type. The top and bottom boundaries were treated
as walls with a no-slip boundary condition.The 2D geometry
was initially meshed with uniform square cells.
A dynamic adaptive mesh refinement in the vicinity of the air–liquid
interface was applied to accurately predict the shape of the interface
and the condition of the confinement. The final shape of the interface
and a representative mesh in the vicinity of the interface is shown
in Figure .
Figure 3
(a) Water volume
fraction contours near the air–water interface
at the end of the simulation and (b) adaptive mesh around the air–liquid
interface in the rectangular area indicated by the dashed line in
(a).
(a) Water volume
fraction contours near the air–water interface
at the end of the simulation and (b) adaptive mesh around the air–liquid
interface in the rectangular area indicated by the dashed line in
(a).A reference case representing
our typical design parameters was
selected for the verification and validation of our numerical work.
In this reference case the heights of the trench and side channels
were chosen as h = 50 μm and H = 200 μm, respectively, where the material of the whole bottom
wall was selected as PDLcG. Experimentally obtained hydrogel solution
contact angles of 31° and 107°, as reported in the Supporting Information, Section 1.4, were employed,
respectively, on PDLcG and PDMS walls. The details of the whole verification
and validation study are explained in detail in the following subsection
(see section: Verification and Experimental Validation
of Numerical Results).
Experimental Setup
Mold
and Device Fabrication
In order to experimentally
validate the CFD model and further support the design with experiments,
STICI3D devices were fabricated out of PDMS elastomer using soft lithography,
and they were plasma-bonded to PDL-coated glass microscope slides.
The PDL coating on the glass provided lower contact angles. The molds
for soft lithographic replication were prepared by utilizing layers
of adhesive polyimide (Kapton) and aluminum tapes to provide height
differences between the side channels and the shallow trench (see
the Supporting Information, Section 1.2).
To obtain a 50 μm trench height (h) and 200
μm side channel heights (H), a layer of aluminum
tape with an inherent thickness of 150 μm was laid over the
first patterned layer of polyimide tape with a thickness of 50 μm.The first layer of adhesive tape (polyimide) was laid over a sheet
of acetate paper and cut into the desired pattern followed by stacking
up the next layer of adhesive tape (aluminum) on top of the previously
cut adhesive tape and cutting into the new desired pattern. Design
patterns (see the Supporting Information, Section 1.1) were cut either manually by a razor or by a digital
craft cutter (Silhouette Cameo, Silhouette America Inc.). Figure a displays a picture
of the produced mold. Keeping the side channel height as H = h + 150 μm, STICI3Ds with trench heights
(h) of 100, 150, and 300 μm were produced with
the same method (see the Supporting Information, Section 1.2).
Figure 5
(a) Mold produced
by adhesive tapes (see the Supporting Information Section 1.2). (b) Water confinement
inside the produced STICI3D with trench height h =
50 μm and side channels H = 200 μm. Areas
filled with Rhodamine B solution in deionized water are seen as pink
(see Movie S2 in the Supporting Information).
Brightfield (c), fluorescent (d), and merged (e) images of collagen
confined within the trench of the STICI3D with h =
50 μm and H = 200 μm. Yellow areas show
the hydrogel dyed with Rhodamine B.
PDMS elastomer (Sylgard 184, the Dow Chemical
Company) base and
curing agent were mixed by a weight ratio of 10:1. The mixture was
thoroughly stirred and desiccated until all the air bubbles were removed.
The mixture was poured into the molds, and the molds were left at
a constant temperature of 55 °C for 3 h for curing. After the
cured PDMS was demolded, the side channel inlet and outlets were formed
using biopsy punchers with 1.5 mm and 2 mm core size diameters, respectively.
Both trench inlet and outlet were punched with a puncher of diameter
2.5 mm. For the cases where high loading pressures were tested, the
inlet diameter of the trench was lowered to 1.5 mm. Heights of the
STICI3D trench and side channels on the demolded PDMS part were measured
by a stylus profilometer (Dektak, Bruker Corp.) (see the Supporting Information, Section 1.3). PDMS and
precleaned PDL-coated glass parts (PDLcG; Menzel Gläser Polysine
slides, Thermo Scientific) were bonded together immediately after
the surface activation by oxygen plasma for 60 s with 100 W radiofrequency
(RF) power under vacuum. After the bonding, postcuring was applied
by placing the STICI3Ds in an oven at 65 °C for 1 h to recover
hydrophobicity and to enhance the bonding strength. STICI3Ds used
in the experiments were all processed by postcuring, unless otherwise
stated.
Preparation and Formation of Hydrogel
The collagen
hydrogel recipe was reformulated based on a recipe from previously
published protocols.[34,35] The ingredients used for the
collagen hydrogel preparation are listed in the order of pipetting
in Table . All ingredients
were stored at 4 °C before usage and kept on ice during mixing.
10X Dulbecco’s Modified Eagle’s Medium (DMEM, F-12 Ham
with 15 mM HEPES and sodium bicarbonate, without l-glutamine,
Sigma-Aldrich Inc.), NaOH (1 M, sodium hydroxide, Sigma-Aldrich),
NaHCO3 (7.5% w/v, sodium hydrogen carbonate, Sigma-Aldrich),
and 1X DMEM solutions and collagen (Type-I, bovine, 6 mg/mL, Sigma-Aldrich
Inc.) were mixed gently to initiate gel formation. Immediately after
mixing, a certain volume of the mixture depending on the trench height
was pipetted from the inlet of the trench. After the collagen-based
hydrogel solution was confined within the trench of the STICI3D, the
devices were left for gelation for ∼1 h in an incubator held
at 37 °C. After hydrogel formation, the STICI3D was ready for
cell seeding. For imaging purposes, the hydrogel was dyed with a fluorescent
dye. Rhodamine B was dissolved in deionized water with a concentration
of 1 mM and was kept at 4 °C before preparing the hydrogel solution.
Four microliters of Rhodamine B (9-(2-carboxyphenyl)-6-(diethylamino)-N,N-diethyl-3H-xanthen-3-iminium
chloride) solution was mixed with 26 μL of 1X DMEM prior to
mixing, constituting ∼5% of the final volume of the hydrogel
solution.
Table 1
Collagen Hydrogel Ingredients
reagents
volume
10X DMEM
5 μL
NaOH 1M
0.5 μL
NaHCO3 (7.5% w/v)
5 μL
1X DMEM
30 μL
collagen Type I
(6 mg/mL)
40 μL
Confinement Tests
Because of the
similar wettability
of collagen solution and water, confinement of the liquid in the shallow
trench of STICI3D was iniatially observed by administering a solution
of Rhodamine B dye dissolved in water. A plasma treatment renders
the PDMS surface hydrophilic. Therefore, the confinement of water
dyed with Rhodamine B was first tested immediately after the PDMS
and PDLcG parts were bonded upon plasma treatment when the surfaces
were still hydrophilic. A 50 μm trench height (h), as in the reference case, was selected for the confinement test
of the STICI3D with hydrophilic walls (see the Supporting Information, Section 1.5 and Movie S1). Second, to promote the hydrophobic recovery of
the surfaces, STICI3Ds were left in the oven at 65 °C for 1 h
after assembly as mentioned in a previous section (see the section: Mold and Device Fabrication). Water confinement
tests after the hydrophobic recovery were conducted with 0 Pa inlet
pressure cases for STICI3Ds with trench heights of h = 50, 100, 150, and 300 μm.In order to observe the
confinement under inlet pressures higher than 0 Pa during a liquid
loading, a STICI3D with a trench height h of 50 μm
was produced with a narrower inlet to the trench so that the conical
tip of the micropipette sealed the inlet entirely (see the section Mold and Device Fabrication).Following
the successful confinement tests with water, hydrogel
solution confinement within the resulting STICI3D platform was investigated.
Rhodamine B fluorescent dye was introduced into the hydrogel mixture
as described in a previous section (see the section Preparation and Formation of Hydrogel). A STICI3D with a trench
height h of 50 μm and side channel height H of 200 μm was prepared for hydrogel solution loading.
The hydrogel confinement in the shallow trench was observed under
an inverted fluorescence microscope (Zeiss Axio Observer Z1) using
a 10× objective. Results of these tests are presented in detail
in the following sections (see the section Collagen
Confinement Tests on Resulting STICI3D).
Cell Studies—Human
Mesenchymal Stem Cell Growth on the
Collagen Hydrogel
Various types of cells can be seeded into
the hydrogel. Among these, mesenchymal stem cells (MSCs) are a subgroup
of stem cells that reside in various tissues and are capable of differentiation
into different cell types.[36] Recent studies
have demonstrated the utility of MSCs as an alternative human cell
source that can be used in engineered platforms recapitulating different
human tissues and organs.[37] A 3D culture
of MSCs affects various properties of these cells, such as phenotype,[38] the proteins that are secreted from these cells,[39] and their differentiation.[40] Hence, MSC chemotaxis has been quantitatively studied in
microfluidic devices.[41]To demonstrate
that the designed STICI3D is suitable for a 3D culture and monitoring
of cells, human mesenchymal stem cells (hMSCs) isolated from umbilical
cords were utilized (see Section 1.6 in the Supporting
Information). According to previously established methods,
the cords were used to form explant cultures of hMSCs.[42] Cell outgrowths from explants were maintained
in DMEM: Nutrient Mixture F-12 containing 10% fetal bovine serum (FBS)
(Biowest), 1% l-glutamine (Gibco), and 0.1% penicillin/streptomycin
(Gibco) (culture medium). The culture dishes were maintained in a
5% CO2 incubator at 37 °C. To enable the cells to
feed and proliferate efficiently, the cell medium was changed every
3 d.Adherent hMSCs were detached from the plates by incubating
the
samples with a 0.05% trypsin-EDTA (EDTA = ethylenediaminetetraacetic
acid) solution (Gibco) for 5 min at 37 °C. The cells were suspended
in the culture medium and counted using a hemocytometer, and 20.000
hMSCs in 10 μL of culture medium were added to one of the side
channels of an STICI3D, in which a collagen hydrogel was formed within
the shallow trench as described above. Following this, the STICI3D
was kept upright for 4 h in a 5% CO2 incubator at 37 °C
to facilitate the cell attachment onto the collagen hydrogel. Thereafter,
both side channels were filled with culture medium, and this was refreshed
every other day.hMSCs placed on collagen hydrogels were fixed
after 3–6
d in the culture. Cells were fixed with 4% paraformaldehyde in phosphate-buffered
saline (PBS) and subsequently stained with phalloidin-FITC (fluorescein
isothiocyanate) (1:200) and with 2-(4-amidinophenyl)-1H-indole-6-carboxamidine (DAPI) antifade solution (Abcam) (1:200).
The stained cells within the STICI3D were imaged using an inverted
confocal microscope (Leica DMi8 SP8) with a 10× objective.
Cell Studies—Culture of Human Umbilical Cord Endothelial
Cells on the Collagen Hydrogel and Treatment with TNF-α
The collagen was loaded onto the STICI3Ds as previously described
(final collagen concentration: 2.98 mg/mL). After 1 h at 37 °C
incubator, HUVEC cells (ATCC) grown in culture medium (culture medium:
ECGM (Lonza) + 5% FBS, penicillin/streptomycin (1000X solution, Gibco)
+ endothelial cell growth supplement; ECGS, Sigma) were trypsinized
(Trypsin-EDTA, Thermo), counted, and seeded (20 000 cells per
middle channel) on the collagen hydrogel. The STICI3Ds were placed
vertically for 4 h to promote cell attachment onto the hydrogel surface.
The culture medium was introduced to both side channels and was further
incubated for 24 h. Tumor necrosis factor alpha (TNF-α, PeproTech)
was introduced at the side channel opposite to the channel containing
endothelial cells at 1 μg/mL concentrations in culture medium.
After 24 h of incubation in the incubator, the live cells were imaged
by loading cells with the live-cell imaging dye; calcein–a
live cell stain. It is introduced to the cells in the acetoxymethyl
ester form (Calcein-AM, Invitrogen); once the ester form enters the
cell, these groups are cleaved, and the free form is fluorescent in
live cells. Upon addition to both side channels, the dye was incubated
for 30 min, enabling access to the cytoplasm. The nonloaded dye was
washed with the culture medium. Images of live cells were taken by
a Leica confocal microscope (Leica DMi8 SP8) in the live cell imaging
mode under 5% CO2 and at 37 °C.
Results and Discussion
Mold and
Device Fabrication
The multilayer adhesive
tape-based mold fabrication presented allowed a reliable, rapid, and
easy method for the fabrication of multilevel channel structures.
The utilization of a sheet of acetate paper as a substrate allowed
the elimination of the silanization step resulting in a significant
reduction in the mold production duration. Moreover, the stacking
up of the adhesive tape layers on top of each other eliminated the
manual alignment requirement of different layers. The production of
mold cut into two layers of adhesive tape (aluminum tape stacked on
top of polyimide tape) for our STICI3D device took less than 4 min
using a craft cutter. The molds were usable up to five times depending
on the level of damage caused during the demolding process.
Verification
and Experimental Validation of Numerical Results
An extensive
numerical verification and validation study on the
reference case that was described in a previous section (see the section Computational Mesh, Boundary Conditions, and Solver Settings) was conducted. In verification study, the mesh and time step sizes
were gradually reduced until the numerical results became independent
of them. After the mesh and time step sizes were determined, the numerical
results of the reference case were compared with the experimentally
obtained data to reveal its accuracy, in the validation study.The mass flow rate from the inlet section of the computational domain
is selected as the dependent flow variable for the mesh and time step
size dependency tests. The change of the inlet mass flow rate for
the reference case is shown in Figure a. The positive inlet mass flow rate indicates that
liquid is sucked from the inlet section into the shallow trench. As
can be seen from Figure a, liquid is sucked from the inlet for a duration of ∼1 ms,
and the mass flow rate converged to a steady-state value of zero,
meaning that liquid is confined. The mesh and time step size dependency
tests were conducted by comparing the average inlet mass flow rate
between 0.0015 and 0.002 s for all test cases. The cell size of the
adaptive mesh at the interface and maximum allowed Courant Number
were selected as independent variables. The results of the verification
study are shown in Figure b,c. A list of maximum Courant Numbers between 0.1 and 2 and
cell sizes between 125 and 2500 nm were selected for these tests.
It can be seen that the solution became independent of Courant Number
and mesh size, at Courant Number of 0.25 and cell size around the
interface of 250 nm, respectively.
Figure 4
(a) Water mass flow rate from the inlet
of the reference case where h = 50 μm, H = 200 μm, r = 0 μm, and Pin = 0
Pa, with PDLcG on middle and side bottom wall. The vicinity of zero
mass flow rate indicating liquid confinement is highlighted in yellow.
Verification study: (b) time step size depedency test results at 250
nm cell sizes near interface and (c) mesh dependency test results
at maximum Courant Number of 0.25.
(a) Water mass flow rate from the inlet
of the reference case where h = 50 μm, H = 200 μm, r = 0 μm, and Pin = 0
Pa, with PDLcG on middle and side bottom wall. The vicinity of zero
mass flow rate indicating liquid confinement is highlighted in yellow.
Verification study: (b) time step size depedency test results at 250
nm cell sizes near interface and (c) mesh dependency test results
at maximum Courant Number of 0.25.Because of the small scales of the channels, the profile of the
air–water interface could not be measured experimentally. The
experimental validation of the study could be made by comparing the
conditions of the confinement of water within the shallow trench.
As mentioned in a previous section (see the section Confinement Tests), the liquid confinement experiment was
performed in a STICI3D with h = 50 μm, using
dyed water as the liquid. The result of a successful water confinement
within the shallow trench is shown in Figure b. (See Movie S2 in the Supporting Information for continuous loading.)
The numerical results shown in Figure a where the inlet mass flow rate converges to zero,
which indicates the interface also converges to a steady-state shape
shown in Figure a
and the water is confined within the shallow trench, are in good agreement
with the experimentally obtained confinement condition.(a) Mold produced
by adhesive tapes (see the Supporting Information Section 1.2). (b) Water confinement
inside the produced STICI3D with trench height h =
50 μm and side channels H = 200 μm. Areas
filled with Rhodamine B solution in deionized water are seen as pink
(see Movie S2 in the Supporting Information).
Brightfield (c), fluorescent (d), and merged (e) images of collagen
confined within the trench of the STICI3D with h =
50 μm and H = 200 μm. Yellow areas show
the hydrogel dyed with Rhodamine B.
Effect of Corner Radius
Because of its small scales,
it is challenging to manufacture microfluidic devices with exact sharp
corners. For instance, in the current study, the corner radius r of a manufactured STICI3D was measured to be r ≈ 5 μm. In order to accommodate for limitations from
a manufacturing standpoint as well, the effect of the corner radius r (highlighted in purple in Figure c) of the shallow trench, where it expands
to side channels, was studied. Water volume fraction contours in the
vicinity of the interface for cases with a sharp and rounded corner
are shown in Figure a,b, respectively.
Figure 6
Effect of corner radius r on liquid confinement,
water volume fraction contours of cases with (a) sharp (r = 0 μm) and (b) rounded corners (r = 5 μm),
where red color corresponds to liquid phase and blue color to gas
phase. A close-up image of the corner area within the dashed line
is shown in the upper-right corner of each figure. h = 50 μm, H = 200 μm, Pin = 0 Pa, PDLcG on middle and side bottom walls.
Effect of corner radius r on liquid confinement,
water volume fraction contours of cases with (a) sharp (r = 0 μm) and (b) rounded corners (r = 5 μm),
where red color corresponds to liquid phase and blue color to gas
phase. A close-up image of the corner area within the dashed line
is shown in the upper-right corner of each figure. h = 50 μm, H = 200 μm, Pin = 0 Pa, PDLcG on middle and side bottom walls.As it can be seen from Figure , a radius of r = 5 μm
causes
only a slight change in the interface shape and does not affect the
confinement. However, since the manufactured actual geometry had a
corner radius of 5 μm, the parametric investigations from this
point forward were conducted with r = 5 μm.
The effect of the corner treatment on the inlet mass flow rate is
shown in the Supporting Information, Section
2.1.
Effect of Trench Height
The liquid confinement within
the shallow trench is maintained by the capillary forces, which are
more dominant than the viscous and inertial forces in microchannels.
As a consequence, the height of the trench h (highlighted
in green in Figure c) becomes a critical design parameter. Therefore, trench heights
from h = 25 μm to h = 300
μm were investigated numerically. The effects of trench height
on the inlet mass flow rate is shown in Figure a.
Figure 7
(a) Effect of trench height on water mass flow
rate at the inlet
boundary. H = h + 150 μm, r = 5 μm, Pin = 0 Pa,
PDLcG on trench and side bottom walls. The vicinity of zero mass flow
rate indicating water confinement is highlighted in yellow. The negative
mass flow rates of h = 200 and h = 300 μm cases shows that the liquid will not be drawn into
the trench by capillary action. Resulting interface shapes at t = 0.002 s for (b) h = 50 μm and
(c) h = 300 μm. Snapshot images of loading
with Rhodamine B solution in deionized water obtained for STICI3D
with (d) h = 50 μm and (e) h = 300 μm. The moment when the pipet tip was retracted from
the inlet of the trench is assigned as t = 0 s. See Movie S2 and Movie S5 in the Supporting Information
for continuous recordings of the loading.
(a) Effect of trench height on water mass flow
rate at the inlet
boundary. H = h + 150 μm, r = 5 μm, Pin = 0 Pa,
PDLcG on trench and side bottom walls. The vicinity of zero mass flow
rate indicating water confinement is highlighted in yellow. The negative
mass flow rates of h = 200 and h = 300 μm cases shows that the liquid will not be drawn into
the trench by capillary action. Resulting interface shapes at t = 0.002 s for (b) h = 50 μm and
(c) h = 300 μm. Snapshot images of loading
with Rhodamine B solution in deionized water obtained for STICI3D
with (d) h = 50 μm and (e) h = 300 μm. The moment when the pipet tip was retracted from
the inlet of the trench is assigned as t = 0 s. See Movie S2 and Movie S5 in the Supporting Information
for continuous recordings of the loading.It is observed from the simulations that, for h =
25 μm to h = 100 μm, the water is
sucked into the trench and is confined. For h = 200
μm and above, the liquid that initially resides within the trench
is pushed back to the inlet of the trench. This result indicates that
the liquid will not be drawn into an initially empty trench by capillary
action. Hence, in order to confine the water within the trench for
more than h = 200 μm, the water must be pushed
with an inlet pressure greater than zero. In a 3D application, although
high inlet pressures can push the interface from inlet to outlet,
it would also push the interface to side channels and could cause
the liquid to overflow. Therefore, the height of the trench was selected
as h = 50 μm, since it is within the range
of confined cases in CFD simulations and is easier to fabricate. The
interface shapes for trench heights h of 50 μm
and h of 300 μm at t = 0.002
s are shown in Figure b,c (see also the Supporting Information, Section 2.2).The numerical results were obtained from a
model that has been
reduced to 2D, and the inlet/outlet sections of the fluids were not
in their actual positions in 3D. In order to further increase the
reliability of the numerical model, an experimental investigation
on the effect of the trench height was performed with STICI3Ds with
trench heights of h = 50, 100, 150, and 300 μm.
The real-time videos of liquid loading processes for STICI3Ds with h = 50, 100, and 150 μm trench heights are provided
in Movies S2–S4 in the Supporting
Information. In parallel with the numerical results, as the trench
height increased, the liquid suction into and through the trench became
harder and slower. Furthermore, for the trench height of h = 300 μm, the immediate liquid suction without an applied
pressure from the inlet was not observed as it is predicted by the
numerical simulations. Figure e demonstrates snapshot images of a liquid loading within
the STICI3D with h = 300 μm. Also see Movie S5 in the Supporting Information for a continuous
recording.
Effect of Bottom Wall Surface Wettability
For a STICI3D
with a hydrophilic bottom wall, adhesion forces pull the air–water
interface from the inlet section to every lateral direction until
water wets the bottom wall completely. However, the cohesion forces
pull the liquid back to the inlet of the trench, and the imbalance
between these forces moves the interface. Where the shallow trench
ends and expands to side channels, a sudden change in the capillary
effect occurs. The top edge of the interface stops at this sudden
expansion region on the top wall, and the bottom edge of the interface
continues to move to the side channels. The interface moves and stretches
until the forces acting on the interface reach an equilibrium and
confine the liquid, as it can also be seen in Figure a.On the one hand, if the contact
angle reduces on the bottom wall, the surface becomes more hydrophilic,
and the force that pulls the interface to side channels increases,
which may cause the liquid to leak or overflow to the side channels.
On the other hand, if the contact angle of the bottom wall increases,
the force pulling the liquid decreases, and the fluid is not drawn
into the trench. The effect of the contact angle of the bottom wall
on the inlet mass flow rate and the condition of liquid confinement
is shown in Figure .
Figure 8
Effect of contact angle of the bottom wall on the inlet mass flow
rate at (a) 0 and (b) 1000 Pa inlet pressure. h =
50 μm, H = 200 μm, r = 5 μm, and Pin = 0 Pa. (insets)
Experimental results of water confinement tests within the STICI3Ds:
(a) confined at P = 0 Pa inlet pressure and (b) nonconfined
under high inlet pressures. See the corresponding Movies S2 and S7 in the Supporting Information.
Effect of contact angle of the bottom wall on the inlet mass flow
rate at (a) 0 and (b) 1000 Pa inlet pressure. h =
50 μm, H = 200 μm, r = 5 μm, and Pin = 0 Pa. (insets)
Experimental results of water confinement tests within the STICI3Ds:
(a) confined at P = 0 Pa inlet pressure and (b) nonconfined
under high inlet pressures. See the corresponding Movies S2 and S7 in the Supporting Information.The results in Figure a show that, as the contact angle increases, the mass flow
rate from the inlet reduces, and for contact angles greater than 45°,
the water retreats from the trench where it initially resides back
to the trench inlet. When the liquid is pushed from the inlet channel
with 1000 Pa, the liquid overflows to the side channel for most contact
angles as shown in Figure b. As the contact angle increases, the forces that pull the
interface to side channels decrease, and for contact angles over 85°,
the water is confined within the trench for inlet pressures under
1000 Pa. Considering the results shown in Figure , using PDLcG rather than plain glass yields
a more robust confinement for liquid loading at 0 Pa inlet pressure,
due to its lower contact angle.The condition of confinement
under 0 Pa and high-pressure loading
cases was investigated experimentally as well. As described in a previous
section (see the section Mold and Device Fabrication), in order to load liquid with higher pressure, STICI3Ds were fabricated
with narrower inlet diameters. When the liquid was pushed gently and
slowly, the liquid was confined within the shallow trench (see Movie S6 in the Supporting Information). However,
when the liquid was pushed by the micropipette faster and stronger,
the liquid overflowed to side channels (see Movie
S7 in the Supporting Information). The experimental results
of confined and overflown cases are also shown in Figure .
Effect of Hydrophilic Surface
Selection
At the current
state of the study, a feasible chip design was developed after the
selections of proper channel height and bottom wall material and after
showing that the manufacturing tolerance at the channel corners does
not affect the liquid confinement condition. However, in the mass
production of the microfluidic devices, failures such as unplanned
high inlet pressures or manufacturing defects might occur. In order
to make the design more resilient against liquid overflow under such
failures, the selection of hydrophilic surfaces was further investigated.Instead of using hydrophilic surfaces for all bottom walls, the
bottom wall of the side channel was selected as PDMS, while the bottom
wall of the trench was selected as plain glass. The zones on the bottom
wall where plain glass and PDMS materials were assigned are shown
in Figure c in red
and blue, respectively. In both cases, where plain glass was assigned
for the whole bottom wall and where plain glass and PDMS were assigned
for the bottom wall of the trench and side channels, they were numerically
tested under various inlet pressures, since both designs successfully
confine the water within the trench under 0 Pa inlet pressure. The
inlet mass flow rates of these designs under various loading pressures
are shown in Figure .
Figure 9
Effect of the selection of hydrophilic surface and corner radii
on the inlet mass flow rate under various inlet pressures. h = 50 μm, H = 200 μm, (a)
plain glass whole bottom wall, r = 5 μm, (b)
plain glass midbottom wall, PDMS side-bottom wall, r = 5 μm. (c) Plain glass midbottom wall, PDMS side-bottom wall
where corners left sharp (r = 0 μm).
Effect of the selection of hydrophilic surface and corner radii
on the inlet mass flow rate under various inlet pressures. h = 50 μm, H = 200 μm, (a)
plain glass whole bottom wall, r = 5 μm, (b)
plain glass midbottom wall, PDMS side-bottom wall, r = 5 μm. (c) Plain glass midbottom wall, PDMS side-bottom wall
where corners left sharp (r = 0 μm).It can be seen from Figure a that water could not be confined for the
design with plain
glass at the whole bottom wall with inlet pressure over 500 Pa. However,
water was confined up to 1500 Pa inlet pressure for the case with
PDMS bottom wall for the side channels as shown in Figure b. These results clearly show
that coating the bottom wall of the side channels with a hydrophobic
material such as PDMS substantially reduces the risk of liquid overflow
into the side channels. The effects of the corner radius on water
confinement were shown in the previous subsection; however, it was
not tested under an inlet pressure higher than 0 Pa. The effects of
the sharp corner on the inlet mass flow rate for various inlet pressures
are shown in Figure c. The comparison of Figure b with 9c shows that a design with
sharp corners successfully confines the water under 2000 Pa inlet
pressure, where the design with rounded corner fails over 1500 Pa.
However, as stated before the effect was minor compared to other design
parameters, and no extra measures were taken to make the corners of
the trench sharper.After a numerical investigation on the effects
of chosen parameters,
the ideal design of the STICI3D was identified to have a trench height h of 50 μm and a side channel height H of 200 μm with PDLcG on the whole bottom wall, even though
using hydrophilic surfaces only at the trench bottom wall reduces
the risk of liquid overflow into the side channels, for the sake of
simplicity in fabrication.
Collagen Confinement Tests on Resulting STICI3D
A STICI3D
with a trench height h of 50 μm and side channel
height H of 200 μm was loaded with hydrogel
solution dyed with Rhodamine B as explained in a previous section
(see the section Preparation and Formation of Hydrogel), and the hydrogel was imaged by an inverted fluorescence microscope
(Zeiss Axio Observer Z1). The image over the whole area of the STICI3D
was obtained by merging the tiles obtained from different locations
over the STICI3D.Figure shows the successful confinement of hydrogel solution within
the trench of the STICI3D. The areas in yellow indicate the locations
of hydrogel dyed with Rhodamine B where side channels were open to
air. Figure c is a
bright-field image, whereas Figure d is a fluorescent-only image of the STICI3D. Figure e displays a merged
image of the overlapping bright-field and fluorescent image.In order to show the 3D profile of the hydrogel, the samples were
also imaged by a Leica DMI8 SP8 confocal microscope with the z-stack
function, and the 3D view was reconstructed by LAS X software (Figure b). The height of
the hydrogel confined within the trench was measured as 52 μm,
which is almost the same as the desired trench height (h = 50 μm).
Diffusion Test through the Hydrogel in STICI3D
To demonstrate
the diffusion process through the hydrogel within the shallow trench
of the STICI3D and the effect of flow rates on side channels on the
diffusion process, four STICI3D chips were produced. For these chips,
a collagen hydrogel solution was loaded, gelated under the shallow
trench, and one of the side channels in each STICI3D was filled with
water. In the first chip, dyed water was loaded to the empty side
channel using a pipet. Dyed water at three different constant flow
rates were infused using a syringe pump for the empty side channels
of the three remaining chips. The image for each of the four chips
was captured exactly 2 min after the liquid within the side channel
reached the center of the side channel, and it is shown in Figure .
Figure 10
Diffusion of dyed water
through the hydrogel inside the shallow
trench under constant flow rates. Mean velocity of the dyed water
is (a) 0, (b) 1V, (c) 10V, and (d)
50V, where V = 185 μm/s.
Diffusion of dyed water
through the hydrogel inside the shallow
trench under constant flow rates. Mean velocity of the dyed water
is (a) 0, (b) 1V, (c) 10V, and (d)
50V, where V = 185 μm/s.It can be seen that the dyed water diffuses through
the hydrogel
and that the side channels are capable of supporting laminar flow
through them. Moreover the chemical concentration gradient through
the hydrogel can be controlled via controlling the flow rate within
the side channels.
Cell-Based Assays Inside the STICI3D
Human
Mesenchymal Cell Culture in Collagen
Collagen
hydrogel was prepared and confined within a STICI3D with a trench
height h of 50 μm, and cells were seeded through
one of the side channels (H = 200 μm). Immediately
after the seeding, as described in the Cell Studies section, the cells were situated on the surface of the hydrogel
facing the side channel onto which they attach and begin to proliferate.
hMSCs interacted with the collagen and migrated into the hydrogel
over time. Figure a shows a 3D reconstruction of confocal microscope z-stack images
of hMSCs grown within the hydrogel in the STICI3D. The red dashed
line indicates the hydrogel to side channel boundary where the left
side of the dashed line is the trench filled with hydrogel. In Figure b, a side view
of 3D-reconstructed confocal microscope stack images of hMSCs is presented.
The two-sided red arrow indicates the total hydrogel region, which
is ∼50 μm.
Figure 11
(a) 3D reconstruction of confocal microscope
stack images of hMSCs
grown in hydrogel within STICI3Ds (h = 50 μm, H = 200 μm), stained with phalloidin-FITC (green for
actin proteins in the cytoplasm) and DAPI antifade solution (blue
for cell nucleus). Red dashed lines indicate the hydrogel-side channel
boundary where the left side is the hydrogel. (b) Side view of hMSC
cells grown in hydrogel within STICI3Ds. Red two-sided arrow shows
the hydrogel region.
(a) 3D reconstruction of confocal microscope
stack images of hMSCs
grown in hydrogel within STICI3Ds (h = 50 μm, H = 200 μm), stained with phalloidin-FITC (green for
actin proteins in the cytoplasm) and DAPI antifade solution (blue
for cell nucleus). Red dashed lines indicate the hydrogel-side channel
boundary where the left side is the hydrogel. (b) Side view of hMSC
cells grown in hydrogel within STICI3Ds. Red two-sided arrow shows
the hydrogel region.Similar reports of MSC
proliferation are present for other microfluidic
platforms.[41,43] These results demonstrate that
the proposed STICI3D platform can support and maintain the 3D culture
of primary cells, such as hMSCs, for a period of 6 d. The data presented
support our aim to produce a microfluidic platform that allows researchers
to image cell growth and migration over extended periods in a biocompatible
hydrogel.
Cellular Response of HUVEC on Collagen Hydrogel
The
functionality of the microfluidic STICI3D was assessed using endothelial
cells placed on a collagen hydrogel, and the effect of adding TNF-α
to the opposing side channel was investigated. TNF-α has been
shown to exert an apoptotic effect on endothelial cells.[44] In our STICI3D, TNF-α is added to the
channel opposite to the seeded HUVECs. The 17.5 kDa protein readily
passes through the hydrogel and affects HUVEC cells, causing cell
death. We followed this by incubating the side channel of the STICI3Ds
with TNF-α for 24 h and assessing cell viability by loading
live HUVEC cells with calcein. In Figure , we show that 24 h of TNF-α incubation
readily diminish viable HUVEC on the side channel, supporting the
functionality of our STICI3D. These results in STICI3Ds indicate that
our design permits a 3D cell culture of various cells; the three parallel
channel conformation enables the delivery of various molecules across
the hydrogel, the experiments being amenable to live-cell imaging.
Figure 12
Experiment
showing the functionality of STICI3D. The collagen was
loaded onto the central channel as previously described, followed
by the seeding of HUVEC cells (20 000 cells per middle channel).
TNF-α was introduced at the channel opposite to the channel
containing endothelial cells at 1 μg/mL concentration in the
culture medium. After 24 h of incubation in the incubator, the live
cells were imaged after cells were loaded with the live-cell imaging
dye; calcein-AM. A Leica confocal microscope took images of live cells
in the live-cell imaging mode under 5% CO2 and at 37 °C.
(a) Control chip. (b) Chip with TNF-α added. This is representative
of five different experiments, each with two chips. Dashed red line
indicates the collagen-side channel boundary.
Experiment
showing the functionality of STICI3D. The collagen was
loaded onto the central channel as previously described, followed
by the seeding of HUVEC cells (20 000 cells per middle channel).
TNF-α was introduced at the channel opposite to the channel
containing endothelial cells at 1 μg/mL concentration in the
culture medium. After 24 h of incubation in the incubator, the live
cells were imaged after cells were loaded with the live-cell imaging
dye; calcein-AM. A Leica confocal microscope took images of live cells
in the live-cell imaging mode under 5% CO2 and at 37 °C.
(a) Control chip. (b) Chip with TNF-α added. This is representative
of five different experiments, each with two chips. Dashed red line
indicates the collagen-side channel boundary.
Conclusions
In vitro cell studies in microfluidic platforms
are proven to be
an effective method due to their ability to mimic, control, and monitor
complex 3D in vivo microenvironments and low volume requirements for
valuable cells and chemical solutions. The geometry and materials
used for the fabrication of such microfluidic platforms play a vital
role to yield a desired microenvironment, since the complex interaction
of mechanical and biological phenomena that take place in microfluidic
platforms is highly dependent on these factors. These microfluidic
platforms are desired to be simple to fabricate, suitable for mass
production, practical to use, and robust, which are achievable through
a meticulous investigation of design parameters.In our study,
we designed a novel easy-to-fabricate microfluidic
STICI3D platform with a simple design that allows the formation of
3D cell cultures inside and on the surfaces of a hydrogel matrix and
precise control of the microenvironment through two side channels
fully in contact with the side surfaces of the hydrogel confined within
the shallow trench where high-resolution microscopic imaging of cells
can be performed. The microenvironment within the hydrogel can be
controlled by two adjacent side channels via diffusion and low-magnitude
convection. In our design, the hydrogel solution can be loaded and
confined within the trench through capillary action without necessitating
micropillars. This shallow trench-induced design allowed us to develop
a simple, easy-to-fabricate device with a continuous and maximized
surface area where chemicals within the side channels interact with
the hydrogel. Our simple design is not only easy to fabricate through
soft lithography techniques using a mold made with adhesive tapes
and razor but also more suitable for mass production methods. In order
to identify the effect of each design parameter, we numerically investigated
the effects of several geometric parameters (channel height, corner
radii) and surface properties (the locations and wettability of the
surfaces) on the confinement of hydrogel solution within the trench
of the STICI3D using CFD simulations.We simplified the geometry
of a numerical model to a 2D cross-section
of the STICI3D thanks to its simple geometric form and simulated the
behavior of an initially confined liquid within the trench under various
inlet pressures for different configurations. We employed a numerical
setup compatible with similar flow problems reported in our previous
studies, and we validated our numerical results by comparing them
with experiments. We have shown that the STICI3D design with a trench
height h of 50 μm, side channel height H of 200 μm, and PDLcG at the bottom wall is the optimum
configuration for the successful confinement of hydrogel solution
within the trench and for fabrication simplicity. With confocal microscopy
results we demonstrated that hMSCs can readily grow and proliferate
in 3D within collagen hydrogels formed within the shallow trench,
supporting the functionality of our novel STICI3D platform. We also
demonstrated that HUVECs lining the collagen respond to the molecules
diffusing through the hydrogel.The easy-to-fabricate nature
and simple design of the STICI3D platform
makes it suitable for researchers interested in fabricating custom
PDMS devices as well as those who are in need of ready-to-use plastic
platforms. As such, the STICI3D in vitro platform has great potential
in imaging cell–cell interactions of multiple cells, angiogenesis,
vasculogenesis, and semiquantitative analysis of drug response in
cells.
Authors: Nak Won Choi; Mario Cabodi; Brittany Held; Jason P Gleghorn; Lawrence J Bonassar; Abraham D Stroock Journal: Nat Mater Date: 2007-09-30 Impact factor: 43.841
Authors: Johnny Lam; Ross A Marklein; Jose A Jimenez-Torres; David J Beebe; Steven R Bauer; Kyung E Sung Journal: SLAS Technol Date: 2017-08-21 Impact factor: 3.047
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