We are describing a method to subject adherent cells to laminar flow shear stress in a sterile continuous flow circuit. The cells’ adhesion, morphology can be studied through the transparent chamber, samples obtained from the circuit for metabolite analysis and cells harvested after shear exposure for future experiments or culture.
The overall goal of this method is to describe a technique to subject adherent cells to laminar flow conditions and evaluate their response to well quantifiable fluid shear stresses1.
Our flow chamber design and flow circuit (Fig. 1) contains a transparent viewing region that enables testing of cell adhesion and imaging of cell morphology immediately before flow (Fig. 11A, B), at various time points during flow (Fig. 11C), and after flow (Fig. 11D). These experiments are illustrated with human umbilical cord blood-derived endothelial progenitor cells (EPCs) and porcine EPCs2,3.
This method is also applicable to other adherent cell types, e.g. smooth muscle cells (SMCs) or fibroblasts.
The chamber and all parts of the circuit are easily sterilized with steam autoclaving. In contrast to other chambers, e.g. microfluidic chambers, large numbers of cells (> 1 million depending on cell size) can be recovered after the flow experiment under sterile conditions for cell culture or other experiments, e.g. DNA or RNA extraction, or immunohistochemistry (Fig. 11E), or scanning electron microscopy5. The shear stress can be adjusted by varying the flow rate of the perfusate, the fluid viscosity, or the channel height and width. The latter can reduce fluid volume or cell needs while ensuring that one-dimensional flow is maintained. It is not necessary to measure chamber height between experiments, since the chamber height does not depend on the use of gaskets, which greatly increases the ease of multiple experiments. Furthermore, the circuit design easily enables the collection of perfusate samples for analysis and/or quantification of metabolites secreted by cells under fluid shear stress exposure, e.g. nitric oxide (Fig. 12)6.
1. Endothelial progenitor cell isolation
2. Shear stress calculation
where Q is the desired flow rate, τ is the target shear stress acting tangentially on the cells, w is the width of the flow chamber, h is the height of the flow chamber, and μ is the viscosity of the perfusate (flow medium).
3. Flow chamber manufacturing
4. Flow circuit assembly
5. EPC fluorescent labeling
6. Cell seeding of slide prior to flow chamber assembly
7. Flow chamber assembly
8. Perfusate sample collection
9. Representative results
Using our quick-seed method, human blood-derived endothelial progenitor cells can be seeded onto titanium slides for 15 minutes and adhere under physiological (arterial) shear forces of 15 dynes/cm2.
As shown in Figure 10, EPCs spread under the influence of flow from 210 ± 11.4 μm2, immediately after seeding, to 657 ± 39.1 μm2 after 3 hours, and to 1152 ± 55.3 μm2 after 24 hours of fluid shear stress of 15 dynes/ cm2 (difference between the groups is statistically significant with p < 0.0001, 1-way ANOVA). Parallel to the increase in cell area, which can be imaged through the transparent chamber with either light or fluorescent microscope, the roundness calculated according to equation 2 6
decreased from 878 x 10-3 ± 5.9 x 10-3, immediately after seeding, to 671 x 10-3 ± 19.2 x 10-3 after 3 hours, and to 526 x 10-3 ± 19.2 x 10-3 after 48 hours of the same fluid shear stress exposure (difference between the groups is again statistically significant with p < 0.0001, 1-way ANOVA).
Figure 11D illustrates that EPCs align and orient in the direction of flow after 48 hours of fluid shear stress at 15 dynes/cm2 as compared to their random orientation after a static seeding period of 6 hours, shown in Figure 11A.
Our method also allows for obtaining samples of the perfusate at predetermined time points for the analysis and/or quantification of secreted cell metabolites. As a representative example we depict the production of nitrite (NO2-) during a 48 hour flow experiment with porcine EPCs in Figure 12. We directly measured this primary oxidation product of nitric oxide (NO) as a surrogate marker for NO in medium samples collected from the flow circuit at the different time points to be 12.0 nmol at 6 hours, 13.1 nmol at 12 hours, 16.3 nmol at 24 hours, and 24.6 nmol after 48 hours for 1 x 106 cells at 15 dynes/cm2 6.
Figure 1. Schematic showing an overview of the flow circuit assembly and flow experiment. (A) Flow circuit assembly without the flow chamber. Included here are the reservoir, pulse dampener, hard tubing, soft tubing, 4-way stopcocks and connected luer adaptors, as well as air filter. (B) Connecting the flow chamber via the hard tubing segment to the flow pump head. (C) Insertion of the EPC-seeded slide into the bottom plate of the flow chamber (D). Complete assembly of the flow circuit with the flow chamber.
Figure 2. Completely assembled flow circuit for sterilization.
Figure 3. Assembled flow circuit after sterilization with stopcocks included.
Figure 4. Filling the glass reservoir with 125 ml of EPC medium.
Figure 5. Flow circuit clamped into the flow pump head prior to flow chamber insertion.
Figure 6. Top chamber plate assembly.
Figure 7. Flushing the bubble trap with EPC medium to remove bubbles from inflow side of the chamber.
Figure 8. Flushing the chamber with EPC medium to remove bubbles from the slide and outflow side of the chamber.
Figure 9. Completely assembled flow circuit with inserted flow chamber during a flow experiment.
Figure 10. EPC area (in μm2) increases over the time course of the flow experiment.
Figure 11. (A) Light microscope image of HUCB EPCs seeded onto a fibronectin coated glass slide x 6 hours prior to flow at 100 x magnification. (B) HUCB EPCs labeled with CTO and quick-seeded onto a Ti slide x 15 min prior to flow, visualized with fluorescent microscopy at 100 x magnification. (C) The same Ti slide with HUCB EPCs as under (B), after 3 hours of flow at 100 dynes/ cm2 and imaged through the transparent chamber at 100 x magnification. Note the spreading of cells but still random orientation after 3 hours of flow. (D) The same Ti slide, now after 48 hours of flow exposure at 100 x magnification. EPCs are labeled with CTO and cell nuclei are stained with Hoechst dye (blue) after flow. Note the alignment of cells in the direction of flow. (E) Porcine EPCs for comparison on Ti after 48 hours of flow and 15 dynes/ cm2 of shear stress exposure. Cell borders were stained with anti-PECAM stain (green) and nuclei with Sytox Orange Nucleic Acid stain. Note the alignment of cells into the direction of flow.
Figure 12. Graph depicts NO production of porcine EPCs during 48 hours of flow. A primary oxidation product of NO, nitrite (NO2-), was measured as a surrogate marker for NO from medium samples collected at different time points during flow.
Figure 13. The flow chamber is made from aluminum alloy 6061 rectangular stock, with the top section (A) being 0.5″ x 2″ x 7″ and the bottom section (B) 0.25″ x 2″ x 7″ in dimension. The top is planed on its underside O-ring contact surface to 0.45″ in order to insure flatness for sealing. The top part is recessed in its center portion to 0.125″, which leaves 0.95″ per end for a 0.3125″ x 1.375″ fluid reservoir. The top section’s reservoir is threaded 3/8-24 T.P.I. and 0.25″ deep to receive threaded stainless steel plugs. Slots measuring 1/16″ x 0.625″ were machined into the underside that penetrate to the reservoir. The inflow side plug has a 10/32″ through hole for a polypropylene 1/8″ hose barb to attach to a stopcock. Each unit end has a centrally located threaded 10/32 T.P.I. by 0.25″ deep portion for a polypropylene 1/8″ hose barb in the 0.45″ x 2″ end. The ends use a 0.07″ hole from the bottom of threads through to penetrate the reservoir. The underside of the top section has a tapered area 0.6875″ wide, 0.518 degrees from the center of an LH slot for a distance of 1.460″. This taper blends to a flat area 0.6875″ wide x 0.0118″ deep and 0.590″ from the end of the glass (or other surface, e.g. titanium slide) recess. This flat must be flush with the glass (or other surface, e.g. titanium slide) once the slide is installed. The taper and flat are polished. The surface of the slide is 0.0118″ recessed from the underside surface. The 0.0118″ recess continues to the reservoir slot on the RH end. An O-ring is recessed entirely around slots and slide leaving 0.020″ of original surface between the O-ring groove and slide. The top and bottom units are drilled for ten holes. The top section has clearance holes for 8/32 T.P.I. countersunk flat head screws. The bottom section has holes placed matching the top holes and are threaded 8/32 T.P.I.. The bottom unit has a clear glass slide window recessed flush with its surface located over the cell surface glass slide (or titanium slide). The unit has an O-ring groove which encompasses slots in the top unit with width to leave 0.04″ of original surface between the bottom slide and the inner O-ring groove. The O-rings are red silicone AS568A, Dash Number 044 for the top section and 046 for the bottom section. Please click here to see a larger version of figure 13.
Our flow circuit and flow chamber allow us to subject adherent cells, e.g. EPCs, to defined fluid shear stresses. Since the chamber top and bottom are transparent, cell adhesion and morphology can be evaluated either in real-time, through the chamber itself, or after a flow experiment and disassembly of the flow chamber. At that point, cells can be harvested under sterile conditions and either re-plated, or used to collect their DNA or RNA, etc., for further analysis.
To achieve laminar flow, the design of the chamber must be such that several conditions are met.
First, the flow must be laminar, which can be verified by calculating its Reynolds number (Re), which is the ratio of inertial forces to viscous forces. (If viscous forces predominate, Re is small and the flow is laminar or ‘fully developed’ – usually for Re < 2300. If inertial forces predominate, the flow becomes more and more random until it is turbulent, as is the case for Re > 4000.) We can calculate Re according to equation 3 8,
Where ρ is the fluid density, Q is the flow rate, μ is the viscosity, w and h are the width and height of the chamber, respectively, and Dh is the hydraulic diameter, defined according to equation 48,
The Reynolds number of our three flow chambers, with heights ranging from 166 – 267 μm, range from 13.9 – 34.6 at flow rates calculated to obtain a shear stress of 15 dynes /cm2. At flow rates calculated for a shear stress of 100 dynes/ cm2, the Reynolds number of the chambers ranged from 90.4 – 234. All of these Reynolds numbers are much lower than 2300 and meet the criterion for laminar flow.
Second, for the velocity field and shear stress to be independent of the distance along the flow channel (i.e. fully developed), the distance from the fluid inlet to slide must be longer than the entrance length, Le. This can be satisfied by calculating the entrance length, according to equation 59.
For the values listed above, the entrance length ranges from 0.01 to 0.25 cm.
Third, in order to ensure that the velocity and shear stress in the lateral direction do not vary significantly from the value for one-dimensional channel flow (ΔPh/2L), the ratio h/w must be much less than 1. For the average wall shear stress under two-dimensional flow conditions to be 95% of the wall shear stress under one-dimensional flow, h/w must be equal to 0.10, and for the wall shear stress under two-dimensional flow conditions to be 97.5% of the wall shear stress under one-dimensional flow, h/w must be equal to 0.05. With the dimensions of our designed flow chamber 1.7 cm in width and 166 – 267 μm in height, these criteria are satisfied.
The pressure will vary only in the direction of flow if there are no lateral pressure gradients at the entrance. This can be assessed using dyes or particles in the flow path. Further, for steady flow experiments, a pulse dampener is inserted in the flow circuit. The pulse dampener takes out most of the pulsatility caused by the roller pump in the circuit, and allows us to approximate the assumption of steady flow. Of note, the pulse dampener utilized should be compatible with the pump and tubing used in the circuit, so that it can effectively eliminate pulsations in the output flow for the specific frequencies of the roller pump. In our demonstration the Masterflex L/S pulse dampener achieves laminar flow when used on the discharge line with any Masterflex L/S series pump (0 – 600 RPMs) and I/P 26 tubing. For pulsatile flow, a programmable pump can be used to generate various waveforms.
For pulsatile flow, a programmable pump can be used to generate various waveforms.
Furthermore, the circuit is designed such that samples of perfusate can easily be collected at different time points without risking contamination of the cells or flow medium. In our example, the concentration of NO2– was measured by chemiluminescence with an Ionics/Sievers Nitric Oxide Analyzer (NOA 280, Sievers Instruments, Boulder, CO) as previously described10. The reductant used for nitrite analysis was potassium iodide in acetic acid (14.5 M acetic acid and 0.05 M KI), which has the reduction potential to convert nitrite to NO but is insufficient to reduce any higher oxides of nitrogen such as nitrate and thus is relatively specific for nitrite. The total amount nitrite produced was calculated as the product of concentration produced and the total volume of the circuit while adjusting for volume lost while taking samples6.
The following steps are critical for the successful execution of flow experiments:
A possible limitation of our flow chamber is that the height is fixed by the height of the channel machined into the aluminum. However, this has the advantage of not having to verify and adjust the height of the channel prior to each experiment and therefore simplifies the shear stress calculations by merely adjusting the pump flow to the desired value. Depending on your research goals, it may be desirable to increase the shear stress without increasing pump speed. In this case we recommend increasing the perfusate’s viscosity, e.g. adding dextran to the medium11.
A possible limitation of the flow circuit is the large volume of medium used, which can be problematic when attempting to quantify very small concentrations of cell metabolites. Though not shown here, it is possible to substantially reduce the circuit volume by using a smaller reservoir and pulse dampener and decrease tubing length and diameter.
Additionally, there are several other commercially available systems that can be used to apply fluid shear stress to cells in culture. Microfluidic-based systems, e.g. the BioFlux system from Fluxion, enable simultaneous analyses of cells in different microfluidic flow channels loaded with solution into well plates acting as input and output reservoirs for these channels12,13,14. However, these and other microfluidic systems are not compatible with standard microscope slides and do not allow for recovery of a sufficiently large number of cells for further experiments, such as RT-PCR or Western Blot. Further, they are less user-friendly, cost a minimum of $40,000 and may reach a total of more than $100,000, depending on accessory equipment.
Two macrofluidic systems available from the Flexcell International Corporation, the Flexcell Streamer and the FlexFlow systems, have been successfully used to study endothelial cells15,16,17, human annulus cells18 and fibroblasts19 under fluid flow conditions. A third system, available through GlycoTech, has been utilized to study tumor cell adhesion20 and leukocyte adhesion21 to endothelial monolayers.
The Streamer system allows several slides to be run under the same shear stress conditions at once, but lacks a viewing window and – unlike our design – does not allow for real-time visualization of cells under flow.
The FlexFlow system has a viewing window, but requires an upright microscope, which might not be the standard microscope used in most laboratories. Further, the FlexFlow system requires a cell-coated cover slip to be inverted when placed into the flow chamber. This precludes visualization of fluorescent cells on an opaque surface, such as titanium-coated glass, which we demonstrate in our study. Lastly, the specialized cover slips need to be purchased specifically for the FlexFlow system, which is in the multi-thousand-dollar price range, similar to the Flexcell Streamer system.
GlycoTech offers circular and rectangular parallel-plate flow chambers, which are significantly less expensive, but manufactured from cast acrylic that cannot conveniently be stem autoclaved like our chamber. Of note, other flow chambers that have been described to be autoclavable appear impractical because they require special microscopic lenses22,23. The GlycoTech system utilizes silicon rubber gaskets interposed between top and bottom plates, which will change in thickness with repeated use and therefore change chamber height over time (the manufacturer recommends purchasing new ones after every ten uses). Our aluminum chamber with built-in O-rings allows for complete opposition of top and bottom plates and ensures constant chamber height between experiments. Lastly, vacuum pumps are necessary to achieve a leak-proof seal in many flow chamber designs, including the GlycoTech chambers, which are not necessary in our design.
Whereas not shown here, the flow chamber can be kept under a microscope during the entire flow experiment for real-time imaging of cell adhesion and/ or behavior. If this is desired, we recommend using heat lamps or a heated pad under the chamber to maintain the perfusate temperature at 37 °C. Further, the roller pump can be replaced with a syringe pump, if no ‘recirculation’ of either cells or metabolites or investigational drugs or agents is desired24.
It is also possible to flow differently labeled cells over adherent cells, e.g. fluorescent platelets over a layer of confluent EPCs (using the platelet assay described by Achneck et al.6,25) to evaluate cell-to-cell interaction under fluid shear stress. Our flow chamber combines valuable features of other available flow chambers, such as a perfusate sampling port and a viewing window and has the important advantage of compatibility with either an inverted or upright microscope. It is fully autoclavable and allows for repeated experiments at constant chamber height and without the need of vacuum pumps to achieve a leakproof seal.
The authors have nothing to disclose.
The authors would like to thank Joe Owen in the Biomedical Instrument and Machine Shop for his tireless efforts in machining and assembling the flow chamber parts and Matt Maudsley from Leica Microsystems for assisting in techniques to image cells through flow chambers. We are indebted to Kevin Collins from Duke Perfusion Services and Dr. Steve Wallace in the Department of Biomedical Engineering for helpful suggestions on flow circuit design. We would also like to thank the National Science Foundation Graduate Research Fellowship Program for supporting Alexandra Jantzen and the NIH for their support through Grant “Autologous EPC lining to improve biocompatibility of circulatory assist devices” RC1HL099863-01.
Products / Reagents | Company | Product # |
10 ml Syringe | Cole Parmer Instrument Co. | 07940-12 |
1-Way Stopcoks | Cole Parmer Instrument Co. | 30600-00 |
30 ml Syringe | BD Medical | 309650 |
4 -Way Stopcocks | Cole Parmer Instrument Co. | 30600-04 |
Aluminum Alloy | N/A | 6061 |
Cell-Culture Dishes (4-well, rectangular) | Thermo Scientific; Nunc | 267061 |
Cell Tracker Orange | Invitrogen | C34551 |
DMSO | Research Organics | 2162D |
DPBS (-/-) | Invitrogen | 14190-144 |
EGM-2 Singlequots | Lonza | CC-4176 |
Female Luer Adaptor | Cole Parmer Instrument Co. | SI-45500-04 |
Fibronectin | Sigma | F0895-2MG |
Glass Bottle (250ml) with Cap | Cole Parmer Instrument Co. | 34594-24 |
Hard Tubing | Cole Parmer Instrument Co. | 06508-16 |
HBSS | Sigma | H8264-500ML |
Histopaque | Sigma | H8889-500ML |
Hoechst Stain Solution | Sigma | H6024 |
Hyclone FBS | Thermo Scientific | SH30071.01 |
L-glutamine | Lonza | 17-605E |
Male Luer Adaptor | Cole Parmer Instrument Co. | EW-45505-04 |
MCDB-131, 1X Medium | Cellgro | 15-100-CV |
Barbed Polypropylene Fittings | Cole Parmer Instrument Co. | 06365-90 |
O-Rings | N/A | AS568A |
Pulse-Dampener | Cole Parmer Instrument Co. | 07596-20 |
Pump-Drive (Masterflex L/S variable-speed economy drive) | Cole Parmer Instrument Co. | 7524-40 |
Pump-Head (Masterflex Easy Load Pump Head) | Cole Parmer Instrument Co. | 07518-60 |
Slide | Cole Parmer Instrument Co. | 48500-00 |
Soft Tubing | Cole Parmer Instrument Co. | 96400-16 |
Syringe filter | Cole Parmer Instrument Co. | 02915-12 |
Sytox Orange Nucleic Acid Stain | Invitrogen | S-11368 |
Trypsin EDTA | Lonza | CC-5012 |
Trypsin Neutralizing Solution | Lonza | CC-5002 |