Method Article
This protocol details the design and fabrication of a microfluidic device suitable for investigating microtubule polymer mechanics. The synthesis of microfabrication, automated flow control, and computational modeling techniques enables a flexible system ideally suited for probing the cellular cytoskeleton in vitro.
In this protocol, we describe the design and fabrication of a microfluidic device developed for the investigation of microtubule polymer mechanics. The design utilizes the intrinsic benefits of Polydimethylsiloxane (PDMS)-based microfluidic devices and introduces several features to enable a robust and customizable high-throughput experimental approach. The developed device incorporates redundant bubble-trapping capabilities to prevent the occurrence of detrimental air bubbles. Furthermore, the device interfaces with an automated flow control system to reduce manual intervention and enable high-throughput analyses. Commercial simulation software is utilized to better develop and understand the fluid transport using this system. Finally, we demonstrate the capability to conduct multiple experiments simultaneously within a single device by growing microtubule extensions with distinct fluorescent labels in different sections of the device. Overall, this microfluidic flow system can be used to probe microtubule polymer mechanics and provides improvements in experimental design for broader microtubule in vitro studies. The synthesis of microfabrication, automated flow control, and computational modeling approaches enables a flexible system ideally suited for probing the cellular cytoskeleton in vitro.
Microfluidics enables precise control of miniscule fluid volumes, often less than one microliter, by the intricate design and fabrication of fluid-flow channels1,2. The small scale of microfluidic devices gives rise to unique engineering phenomena. Namely, the Reynolds number-a dimensionless measure of the ratio between inertial and viscous forces in fluid flow-is small, typically on the order of O(10) or lower in microfluidics, underscoring the importance of viscous forces in microfluidic devices. Additionally, the Péclet number, which compares convective to diffusive transport, shows that convective transport is generally negligible in microfluidics3,4,5. This diffusion-driven, laminar flow regime in microfluidics is advantageous, as it supports parallel experiments on a single device by maintaining precise fluid gradients.
Photolithography remains the primary method for fabricating microfluidic devices6,7,8. In brief, this process involves creating a 'master' etched template of the microfluidic design (Figure 1). A photosensitive substrate is prepared, and a photomask of the microfluidic design selectively exposes areas of photoresist to ultraviolet radiation. Subsequent etching methods develop the substrate, producing a relief of the design. Polydimethylsiloxane (PDMS) is often cast and cured onto the master. The cured PDMS, which adopts the negative features of the design, is then removed from the master and bonded to a glass coverslip. This entire fabrication process typically takes 1-2 days, enabling quick design iterations and the production of multiple devices. Detailed reviews of soft lithography and microfabrication processes are available in other references1,2,3,10,11,12,13.
Figure 1: Overviews of the traditional photolithography process and microfabrication process. (A) Traditional photolithography process and (B) microfabrication process. Depending on the application and desired photoresist characteristics, a negative or a positive photoresist can be used, even though they will yield the same design master. Characteristics such as feature height desired or photoresist melting temperature help determine the appropriate photoresist type. This figure has been modified with permission from Rogers (2022)14. Please click here to view a larger version of this figure.
The use of microfluidics has expanded the possibilities in many research fields, with its most recent impact being in the biological sciences. Given its small scale, microfluidics allows for the precise management of limited, valuable resources such as cells or proteins. Even more impactful is the tunability of microfluidic systems to mimic physiological conditions, such as modifications in substrate stiffness, the exertion of force on a specimen, and even the integration of electrical current. Additionally, the use of microfluidics offers the ability to manipulate multiple reagents in parallel and to rapidly prototype and iteratively refine system designs. These features enable the miniaturization of entire laboratory workflows onto a single device, commonly referred to as a "lab-on-a-chip"1,6,9,15,16,17,18,19.
One of the cell-biological applications of microfluidics is investigation of microtubule polymers. Microtubules are an essential component of the cell's cytoskeleton, playing a vital role in processes such as cell division and intracellular cargo transport20,21. As the most rigid element of the cytoskeleton, microtubules exhibit an elastic modulus comparable to that of Plexiglass22,23. Their robust mechanical properties are crucial for various cellular functions, including, for example, cardiomyocyte contraction, where they cyclically bend and relax during the heart's systolic and diastolic phases24. Microfluidic devices have been previously adopted to investigate the properties of microtubules and their higher-order structures in vitro. Indeed, microfluidics has been used to probe microtubule polymerization dynamics, microtubule-microtubule interactions, and the effects of microtubule-associated proteins on microtubule mechanical properties25,26,27,28,29,30,31,32,33,34,35,36,37,38,39,40,41.
While the introduction of microfluidics into the microtubule field has brought about many exciting discoveries, room for improvement still lies in the adaptation of these devices for microtubule research. In this work, we address two specific limitations that persist in studying microtubules in microfluidic devices: the potential for air bubble formation within the device, typically introduced by manual manipulation of microfluidic devices, and the underutilization of high-throughput assays. First, manual manipulations, such as plugging and unplugging tubing, can introduce bubble formation into channels. Air bubble formation within a flow cell is catastrophic, as air bubbles can denature proteins, shear microtubule polymers, and adversely affect cell cultures42,43. In addition, sharp corners and oblique angles in the device result in non-uniform surface wetting, increasing the possibility of air entrainment. Numerous techniques have been developed to reduce the formation, persistence, and impact of air bubbles; however, the use of bubble mitigation methods is not universal42,43,44,45,46. Furthermore, although one of the major advantages of using microfluidics is the ability of high-throughput experimentation, microfluidics has not yet been used to scale-up microtubule research. Microfluidic devices can be designed to test multiple experimental conditions in parallel on the same device. For example, fluid gradients can be used to direct the flow of different microtubule-associated proteins or drugs, enabling their targeted delivery to specific regions of partitioned microtubules within the same device.
Here, we iteratively designed a microfluidic device that addresses these limitations. We provide the step-by-step protocol of the fabrication of the device, thereby enabling a wider audience to employ microfluidic technology in their microtubule research. This device design incorporates bubble-trapping features and utilizes an automated flow control system to reduce manual intervention while also enabling gradients of solutions in the device for high-throughput analyses. In summary, the development of this microfluidic design can facilitate broader research and understanding of microtubule mechanics while offering valuable improvements to experimental designs across the broader microtubule research field.
NOTE: The work detailed in this portion of the protocol was performed in the Vanderbilt Institute of Nanoscale Science and Engineering (VINSE) core Class 100 cleanroom. A controlled cleanroom with appropriate gowning and UV-filtered lighting is desired to prevent device damage due to humidity/ambient lighting conditions and to prevent particulate contamination. All manipulations on silicon wafers should be done with the silicon wafer polished side facing up. Use tweezers when manipulating wafers and minimize touching surfaces of the wafer to prevent scratching. Keep wafers in Petri dishes with the lids covered when transporting and at the end of each day unless otherwise directed.
1. Photolithography (6 - 8 h)
2. Development (1 - 2 h)
3. Silanization (1 - 2 h)
4. PDMS deposition (1 - 2 h)
NOTE: If there is residual PDMS on the master from a previous microfabrication, the residual PDMS must be removed prior to depositing new PDMS.
5. PDMS device assembly (1 - 2 h)
6. Microfluidic flow channel preparation (1 h)
Order | Reagents | Volume Dilution | Wash Volume | Incubation Time |
1 | BRB80 | N/A | 50 μL | N/A |
2 | Anti-rhodamine antibody | 1:50 in BRB80, mix well | 25 μL | 5 min |
3 | BRB80 | N/A | 50 μL | N/A |
4 | Poloxamer 407 (F127) | 1% in BRB80 | 25 μL | 15 min |
5 | BRB80 | N/A | 50 μL | N/A |
Table 1: Order of preparation of microfluidic device channels.
Volume | Reagent | Stock Concentration | Final Concentration |
16 μL | D-Glucose | 2 M | 80 mM |
16 μL | Glucose Oxidase | 2 mg/mL | 80 μg/mL |
16 μL | Catalase | 0.8 mg/mL | 32 μg/mL |
14 μL | Casein | 28 mg/mL | 0.16 mg/mL |
8 μL | DTT | 1 M | 20 mM |
40 μL | Potassium Chloride | 1 M | 100 mM |
290 μL | BRB80 | 1x | N/A |
400 μL | FINAL (2x working concentration) |
Table 2: Antifade imaging solution recipe (2x concentration).
7. Introduction of microtubule seeds to microfluidic (10 - 15 min)
8. Growing microtubule extensions from seeds (15 - 30 min)
9. Stabilizing microtubule extensions (10-15 min)
10. Bending stabilized microtubule extensions (10 - 15 min)
NOTE: Stabilized microtubule extensions can now be bent using a flow controller. Here, a regulated, positive-pressure displacement system (Elveflow OB1 MK3+) was used to flow the solution from an airtight source vial through a flowmeter and into the microfluidic. Depending on the specifics of the available flow controller setup, modifications may be made to the following steps.
Microfluidic device design rationale
The design of the microfluidic device in this study was guided by several key features (Figure 2), which build and improve upon the traditional simple flow-cell design. Of note, the microfluidic device has an internal volume of ~160 nL, significantly smaller than the ~10 µL volume of more traditional flow cells47, allowing for a more controlled use of potentially precious reagents, such as purified protein components. Because the microfluidic flow controller contains two regulating channels, the device was developed assuming that only two inlet/outlet ports would have pressure control at any given time. More pressure-controlled channels can be implemented, if desired.
Figure 2: Schematic of the microfluidic device design. Rectangular markings on the periphery are for visual aid in seeing the periphery of the channels. Please click here to view a larger version of this figure.
The central, rectangular device chamber serves as the main imaging area where microtubule seeds are attached, and microtubule extensions are polymerized off of these seeds. The chamber is intersected by a flow channel on each side, with straight channels along the x-axis serving as an inlet and outlet to facilitate rapid exchange of the reaction solution. Microtubule inlet channel is also used to introduce microtubule seeds into the chamber, with laminar flow resulting in the seed binding to the glass surface along the direction of flow. In the perpendicular (y-axis) direction, the flow channels branch into smaller channels towards the chamber, similar to some of the previous designs25,28,36,39. The branching geometry is particularly suitable for studying the mechanical properties of microtubules. Flowing a solution into the central chamber from a direction perpendicular to the orientation of the microtubule seeds allows for flow-induced bending forces at near-normal angles. Furthermore, the inclusion of branching geometry with many smaller flow channels facilitates a more homogeneous force application over a wide area of the central chamber, which is not achieved by a simple single-channel flow geometry. In this way, the branching motif, while seemingly more complicated, can reduce overall complexity in determining the force imparted to microtubules (Figure 3). This design also features multiple lines of symmetry, allowing for ease of use and the opportunity to evaluate bending from several directions (e.g., top vs. bottom).
Figure 3: Inclusion of a branching motif results in a large area of similar flow. Simulations of two device designs under steady-state flow: one without branching channels (A) and one with branching channels (B). Arrows denote local flow direction and are proportional to flow magnitude. Surface coloration denotes centerline velocity. Images on the right show zoomed-in section of the device where microtubules (not shown) oriented along the x-axis would be subject to bending forces from a fluid flowing in the top port and out the bottom port. Incorporating branching channels increases the relative area subject to similar velocity fields while not increasing the volume of reagent required. This figure has been modified with permission from Rogers (2022)14. Please click here to view a larger version of this figure.
Notably, the device also implements a series of bubble traps in the inlet and outlet flow channels to prevent air bubbles from entering the central imaging chamber. Specifically, we chose to include arrays of micropillars within the flow path in order to block air bubbles from traveling past due to surface tension (Figure 2)46. Furthermore, to prevent air entrainment, we designed the edges inside the device as smooth curves, as opposed to having oblique angles. Taken together, these design features reduce the possibility of air bubbles and increase the robustness of the device.
Microfluidic device fabrication
Determining the proper parameters for creating the device master required some optimization. As previously observed, this photoresist is very sensitive to key operating parameters such as ambient lighting and the rates of heating and cooling during the photolithography steps50. For example, if the master was cooled too quickly after heating, thermal cracks could develop in the photoresist. This is undesirable, as the cracks can compromise channel integrity. While cracks could be resolved by re-heating the resist to a temperature near its transition temperature (~115 ˚C), we found that allowing the master to ambiently cool on the hot plate was the most robust way of preventing cracking. Furthermore, excess ambient light can result in unintended exposure of the photoresist, weakening the resist and resulting in the device features themselves (which should remain on the wafer after development) undergoing partial stripping away during the development step. For this reason, we encourage the development step to be performed the day after the post-exposure baking and ambient overnight cooling steps. Moreover, whenever the device master is not in use, we recommend storing it in a dark area or wrapped in aluminum foil to prevent degradation over time. Once these parameters were determined, the photolithography process was highly repeatable (Figure 4).
After the master was created, liquid PDMS was cast on top of the master, allowing the PDMS to cure and create a negative imprint of the master's features. We found that casting the PDMS at a thickness of 2-3 mm allowed for easy manipulation of the devices; in contrast, if spin-coated to achieve a thickness in the µm range, the PDMS was prone to tearing or self-adhering, making manipulation difficult. Furthermore, a thicker PDMS layer allows for easier plugging in of tubing, as the tubing will remain in the inlet/outlet ports without the need for a sealant or clamp.
Finally, while traditional flow-cell assays for these biological applications often use glass coverslips that have been pre-cleaned using a Piranha solution (hydrogen peroxide and sulfuric acid) and then silanized, we found that coverslips treated with an extended plasma clean and IPA wash were suitable for our purposes47. Other applications, such as single-molecule imaging, may require a more extensive cover glass treatment.
Figure 4: Photolithography process. (A) The mask with the desired design (mask made from chromium etched on glass). (B) Slight cracking of photoresist on the silicon wafer due to thermal stress (arrows highlight a few cracks). These cracks often stretch across the entire wafer. (C) The developed master. (D) The microfluidic setup on the microscope. Individual components are labeled in green. Please click here to view a larger version of this figure.
Microtubule growth, stabilization, and bending
GMPCPP-grown microtubule seeds serve as nucleation sites for microtubule extensions to polymerize and are themselves stable against depolymerization for several hours at room temperature. The seeds were bound to the glass coverslip in the microfluidic channel using an anti-rhodamine antibody47. Dynamic microtubule extensions were then grown in the presence of soluble tubulin (fluorescently labeled but not rhodamine-conjugated) and GTP. In this way, the seed nucleation sites were attached to the glass coverslip, but the extensions were not. During the 15-min extension growth period, microtubule extensions polymerized and depolymerized stochastically, as expected due to their intrinsic dynamic instability49. Following this growth period, a 10 µM Taxol washout was carried out to eliminate any remaining tubulin from the solution and stabilize the microtubule extensions that had formed. The stabilization is key, as the microtubule extensions would otherwise depolymerize upon tubulin depletion. In addition to binding and stabilizing microtubule polymer, Taxol has also been demonstrated to impact microtubule polymer mechanics and may induce curvature in the otherwise linear microtubule extensions51,52,53,54. The results shown here reflected these observations; however, the curling of the microtubule extensions is undesirable, as this results in uneven forces imparted along the lattice during bending. Therefore, only microtubules that remained relatively straight after stabilization were used for bending analysis. Alternatively, after the initial growth period, a secondary growth period with a solution of tubulin and GMPCPP (as opposed to the initial GTP) can be used to create stable 'caps' on the growing ends of the microtubule lattice and prevent depolymerization55.
Microtubules were then bent by flowing in the buffer solution using the pressure control system to maintain a constant upstream pressure (Figure 5, Supplementary Video 1). In this way, we could approximate the local flow experienced by the microtubules. By flowing fluid in from the top and out of the bottom device port, the orientation of the flow was intended to be perpendicular to the seeding orientation.
Figure 5: The microfluidic setup can be used to bend stabilized microtubules. Microtubules in a resting state after stabilization with paclitaxel are bent during pulsatile flow. A constant upstream pressure of 30 mbar drives flow (arrow denotes direction of flow). Please click here to view a larger version of this figure.
Determination of flow profile in the microfluidic device
The centerline velocity in the microfluidic can be computationally simulated using COMSOL software (simulation software, Figure 6A). However, the microtubules are attached to the glass coverslip for TIRF microscopy within ~100 nm of the surface. Therefore, the velocity experienced by the microtubule is not the same as that predicted in the 2D simulation. To approximate the local flow experienced by the microtubules, we used the general Navier-Stokes equation for an incompressible fluid flow in one dimension:
Here, z is the height of the microtubules in the device, h is the overall height of the device, and vc is the centerline velocity in the device. By definition of the system, the z-origin is the center of the device (Figure 6B). Using this definition and a channel height of 13 µm, the height of the microtubules is approximated as z = -6.4 µm. Solving this equation yields an estimate for the local fluid velocity experienced by the microtubules:
Figure 6: Defining the system for fluid flow analysis of fluid entering the device at the top port and exiting at the bottom port (ports not shown). (A) Simulation of scaled centerline velocity field as in Figure 3B. Star denotes the area of interest for panel B. (B) Cross-sectional representation of the device. Fully developed fluid flow profile is in the y-direction with a centerline velocity vc at z = 0 and a no-slip boundary condition at the walls. Note that the arrows in this panel are not to scale with respect to the actual velocity field shown in panel A. This figure has been modified with permission from Rogers (2022)14. Please click here to view a larger version of this figure.
Beyond simulations, fluid velocity can be controlled using a flow controller based on a volumetric flow rate rather than maintaining pressure. Furthermore, the local flow rate in each device can be directly determined by including fluorescent beads and monitoring their velocity, thus alleviating any sample-to-sample variability.
Computational modeling and gradient demonstrations
Finally, we performed computational simulations in combination with experiments to demonstrate the feasibility of using this device for high-throughput experiments. Along with the ability to bend microtubules in multiple directions thanks to the device's symmetry, the simulations showed that the device can maintain precise gradients, enabling the simultaneous investigation of multiple experimental conditions (Figure 7A). Preliminary experiments (methods not explicitly stated as part of this publication) using fluorescent dye in solution demonstrated consistency with the computational predictions (Figure 7B). Furthermore, we successfully demonstrated the partitioning of different proteins in different areas of the device by simultaneously growing microtubule extensions with different fluorescent labels (Figure 8). To our knowledge, this is the first application of high-throughput microfluidics to microtubule investigations. This feature of this device can be used to reduce the time and quantities of needed reagents while also improving experimental robustness. For example, the effects of different proteins or distinct concentrations of individual proteins on microtubule mechanics and dynamics can be simultaneously investigated simultaneously in a single device.
Figure 7: Gradient formation. (A) Simulation of a gradient of two solutions entering the device at the same inlet pressure (50 mbar) and concentration (15 µM). Inlet ports for each solution are denoted with colored arrows (one solution in the top port and another solution in the right port), and the two remaining ports serve as outlets. Heatmap shows the concentration profile of the top solution. Steady state was achieved at t = 5 s. (B) Experimental generation of a similar gradient using fluorescent dye in solution in the top port and buffer in the right port. Image is a raster layer made by stitching each field of view (80 µm × 80 µm) to resolve the entire device area. This figure has been modified with permission from Rogers (2022)14. Please click here to view a larger version of this figure.
Figure 8: Demonstrating a protein gradient in the microfluidic device. AlexaFluor647 labeled tubulin (magenta) was flown in inlet 1, and AlexaFluor488 labeled tubulin (green) was flown in inlet 2 of the device at equal concentrations and flow rates. Flow was oscillated on/off in 90 s increments to allow for tubulin polymerization from stabilized-GMPCPP seeds (red) while inhibiting mixing. (A) Large-scale raster layer made by stitching fields of view (80x80 µm) to resolve the entire length of the device. Letters designate the relative location of individual fields of view in subsequent panels. Scale bar is 50 µm in X and Y-position. (B) Field of view near inlet 1 of the device, where extensions are comprised predominately of A647-labeled tubulin. (C) Field of view near the middle of the device, where extensions are comprised of a mixture of labeled tubulins, as predicted. (D) Field of view near the bottom of the device, where extensions are comprised predominately of A488-labeled tubulin. Please click here to view a larger version of this figure.
A process flow diagram (PFD) for the microfluidics experimental setup on a microscope is shown in Supplementary Figure 1.
Supplementary Figure 1: A process flow diagram (PFD) for the microfluidics experimental setup on a microscope. Please click here to download this File.
Supplementary Video 1. The microfluidic setup can be used to bend stabilized microtubules. Microtubules in a resting state after stabilization with paclitaxel are bent during pulsatile flow. A constant upstream pressure of 30 mbar drives flow. Video playback rate 10 fps. Please click here to download this File.
Supplementary File 1: A CAD file of the microfluidic mask design. Please click here to download this File.
The primary goal of this protocol was to design and fabricate a microfluidic device suitable for the investigation of microtubule mechanics in vitro. The design was based on the desire to utilize the intrinsic benefits of PDMS-based microfluidic devices while also including a combination of features that would enable robust and customizable high-throughput experimentation.
This goal has been successfully achieved, resulting in fabrication protocols and general guidelines that can serve as a basis for future users of this system. The inclusion of redundant bubble traps in the device decreases the likelihood of protein denaturation due to the presence of air bubbles. While we still have some unplugging and re-plugging of tubing in the device, these bubble traps reduce the probability of experimental failure. Future improvements to the microfluidic setup could even further reduce the amount of manual tubing manipulations made during an experiment. Moreover, the integration of the microfluidic device with an automated flow control software allows for a significant customization of experimental conditions while reducing the possibility of manual error. We have demonstrated the device's successful performance by fabricating the device and then growing, stabilizing, and bending microtubule extensions in the device using automatic, controller-regulated flow. Furthermore, by establishing a gradient of distinct fluorescently labeled tubulin solutions within the same device, we showed that multiple conditions can be run simultaneously in a single device. Aided by computational modeling and analysis techniques, our system can probe and determine the biomechanical properties of microtubules, such as flexural rigidity52,56,57,58,59.
Potential future improvements would facilitate an even more robust system and associated experimental analysis. First, the photoresist deposition, exposure, and baking were crucial parameters that demonstrated some variability. The relatively tall feature sizes of the SPR photoresist required very gradual heating and cooling to prevent thermal cracking, which could ruin the devices. While thinner devices were attempted, we found issues with the manipulation of these smaller feature sizes. Attention to detail and patience are crucial for replicating devices of this thickness with SPR photoresist. Different photoresists may be used to solve this issue, depending on availability.
Taken together, the microfluidic device and protocol here allow for a range of experimental setups with more robust, high-throughput testing capabilities than previous flow-cell assays47. Furthermore, experiments can be automated using flow controllers to maintain precise flow profiles or concentration gradients in the device, reducing variability inherent to manual users. Future potential applications of this setup include investigating the effects of microtubule-associated proteins on microtubule flexural rigidity, dynamics, lattice damage, and repair, as well as the biomechanical interactions of microtubules and actin filaments54,60,61,62,63,64,65,66,67,68,69,70. The integration of microfabrication, automated flow control, and computational modeling and analysis techniques creates a versatile system suited for studying the cellular cytoskeleton in vitro.
The authors have no conflicts of interest. The authors disclose the use of ChatGPT-4o OpenAI for text revision and proofreading.
We are grateful for the support and resources provided by the Vanderbilt Institute of Nanoscale Science and Engineering (VINSE), where a portion of this research was conducted. This work was partially funded through an NIH NIGMS grant to M. Zanic (R35 GM1192552) and NSF ID 2018661 grant to M. Zanic. M. Rogers received support from the NIH T32 GM08320 grant and a VINSE pilot funding award. L. Richardson is supported by the NSF GRFP Grant No. 1937963. The authors would also like to thank Dr. Alice Leach, David Schaffer, Dr. Christina McGahan, and the entire Zanic lab for their assistance and support.
Name | Company | Catalog Number | Comments |
0.6 mL microcentrifuge tubes (clear) | Any brand | Low retention type is preferred | |
1.5 mL microcentrifuge tubes (clear) | Any brand | Low retention type is preferred | |
1.5 mm standard biopsy punch | Integra LifeSciences | 33-31A-P/25 | |
100x/1.49 numerical aperture TIRF objective | Nikon | ||
22 x 22 mm glass coverslips | ThorLabs | CG15CH | |
3" single side polished silicon wafers | University Wafer | 447 | |
4" Petri dish | Any brand | ||
450 µL, Open-Top Thinwall Ultra-Clear Tube | Beckman Coulter, Inc. | 345843 | Referred to as 'airfuge tube' in the protocol |
488-, 561, and 640-nm solid state lasers | Nikon | ||
A-95 Fixed-Angle Rotor | Beckman Coulter, Inc. | 347595 | |
Acetone | Any brand | ||
Airfuge Air-Driven Ultracentrifuge | Beckman Coulter, Inc. | 347854 | Referred to as 'airfuge' in the protocol |
Alexa Fluor 488 Microscale Protein Labeling Kit | Thermo Fisher Scientific | A30006 | |
Aluminum foil | Any brand | ||
Andor iXon Ultra EM-CCD | Nikon | ||
Andor NEO sCMOS | Nikon | ||
AutoCAD | Autodesk | Generic versions can be used | |
Bovine brain unlabeled tubulin (purified) | N/A | Made in house, but can be purchased | |
Casein | MilliporeSigma | C7078 | |
Catalase | MilliporeSigma | C9322 | |
Clean Dry Air (CDA) (pressurized gas) | Any brand | ||
Compressed air supply | Any brand | Connects to the microfluidic flow controller | |
COMSOL Multiphysics software | COMSOL, Inc. | ||
Custom brass stage adapter | N/A | Made in house to fit our 22 mm x 22 mm coverslips onto the microscope | |
De-ionized water | Any brand | ||
Dessicator | Any brand | ||
D-glucose | MilliporeSigma | G7528 | |
Dithiothreitol (DTT) | MilliporeSigma | D0632 | |
EGTA | MilliporeSigma | 324626 | |
Elveflow Smart Interface (ESI) software | Elveflow | ||
Flangeless PFA fittings with ETFE ¼”-28 to 1/16” outer diameter ferrules | Darwin Microfluidics | CIL-XP-245X | Used to connect the tubing from the micrewtube source vials to the flow sensor via the pressurized reservoir rack |
Fluiwell 4-Channel 2 mL Low Pressure | Fluigent | 14002001 | Used to connect the flow control system to the the micrewtubes. Also refered to as 'pressurized reservoir rack' |
Fume hood | Any brand | ||
Glucose oxidase | MilliporeSigma | G6125 | |
GMPCPP | Jena Bioscience | NU-405L | |
Guanosine triphosphate (GTP) | MilliporeSigma | G8877 | |
Hot plate | Any brand | ||
HS-625 high-speed emission filter wheel | Finger Lakes Instrumentation | ||
ImageJ software | N/A | Open access | |
Incubator | Any brand | ||
Isopropyl alcohol | Any brand | ||
Karl Suss MA-6 mask aligner | SUSS MicroTec | ||
Magnesium chloride | MilliporeSigma | 1.05833 | |
MATLAB software | MathWorks | ||
MEGAPOSIT SPR 220 7.0 photoresist | Dow, Inc. | ||
Microfluidic Fittings 6-40 to 1/4"-28 Adapters Kit | Darwin Microfluidics | LVF-KFI-08 | Used to connect the tubing from the micrewtube source vials to the flow sensor via the pressurized reservoir rack (Fluiwell rack) |
Microfluidic Fittings Female Luer Lock Adapter Kit | Darwin Microfluidics | LVF-KFI-04 | Used to connect the syringe to the tubing |
Microfluidic flow controller | Elveflow | OB1 MK3+ | |
Microfluidic flow sensor | Elveflow | MFS3 | This flow sensor range is 0-80 μL |
MICROPOSIT MF-319 developer | Dow, Inc. | ||
Microscope | Nikon | Eclipse Ti | |
NIS-Elements software | Nikon | ||
Nitrogen (pressurized gas) | Any brand | ||
Objective heater | Tokai Hit | ||
One-Piece Fingertight 10-32 Coned Fitting for 1/16" OD Tubing | Darwin Microfluidics | CIL-F-120X | Used to connect the syringe to the tubing |
Paclitaxol (Taxol) | Tocris Bioscience | 1097 | |
Photolithography masks | N/A | Made by an external party using our designs | |
PIPES | Thermo Fisher Scientific | 172615000 | |
Plasma cleaner | Harrick Plasma | PDC-32G | |
Plasma flowmeter system | Harrick Plasma | PDC-FMG | Integrates with plasma cleaner to enable flow control of pressurized gas |
Plastic bulb pipet | Any brand | ||
Pluoronic F-127 | MilliporeSigma | P2443 | Referred to as 'poloxomer 407' in the protocol |
Potassium chloride | Research Products International | P41000 | |
Saint Gobain Performance Plastics Tube Tygon .020 ID | Thermo Fisher Scientific | 50-206-8921 | Refered to as '1.5 mm tubing' and 'tubing' in the protocol |
Scalpel | Any brand | ||
Spin coater | Cost Effective Equipment, LLC. | 200x | This model may be discontinued |
Standard pipets and tip sets | Any brand | ||
Standard plastic syringe | Any brand | We used a 10 mL Luer-slip syringe | |
Sylgard 184 silicone elastomer kit | Dow, Inc. | Referred to as 'PDMS' and 'curing agent' in the protocol | |
T339 Micrewtube with Lip Seal and Flat Screw Cap | Medline Industried, LP. | T339 | Referred to as 'source vial' in the protocol. We used both 0.5 mL and 1.5 mL sizes |
TAMRA, SE; 5-(and-6)-Carboxytetramethylrhodamine, Succinimidyl Ester | Invitrogen | C1171 | Referred to as 'TTR' in the protocol |
Trichloro(1H, 1H, 2H, 2H-perfluorooctyl) silane | MilliporeSigma | 448931 | |
Trion Phantom RIE ICP | Trion Technology, Inc. | This plasma cleaner is only used in Step 1.1 of the protocol. Another plasma cleaner, like the one used for PDMS bonding, can be used instead; we just prefer the much lower vacuum achievable by this system for cleaning the silicon wafer | |
TRITC Polyclonal Antibody | Thermo Fisher Scientific | A6397 | Referred to as 'anti-rhodamine antibody' in the protocol |
Tweezers | Any brand | ||
Vacuum pump | Any brand |
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