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International Journal of Bioprinting                 Impingement shear stress during microvalve-based bioprinting




































            Figure 2. Validation of the simulation model. (a) Simulation model predicts dispensing dynamics similar to that captured by HSC during 2000 µs. Scale
            bar: 1 mm. (b) Maximum wall shear stress inside the nozzle varies slightly by different mesh sizes (course, medium, and fine). Medium mesh size was used
            for follow-up simulations. (c) Similar maximum wall shear stress inside the nozzle was predicted by numerical simulation using different time steps of 12.5,
            25, and 50 ns (results are overlapped). Therefore, 25 ns was used for follow-up simulations.

            captured by HSC. The experiment was conducted using
            a SMLD 300G-300 µm microvalve. The opening time of
            the valve was set to 400 µs with an upstream pressure of
            1.0 ± 0.1 bar. The distance between the platform and nozzle
            was set to 1.20 ± 0.06 mm in the experiment. These same
            values were implemented in the simulation model (details
            of  the  geometry  and  numerical  model  are described  in
            section 2 and Supplementary File). The simulation results
            predicted a droplet/jet formation dynamic similar to
            that captured by HSC during the experiment (Figure 2a;
            Videoclips S1 and S2 in Supplementary File). A total time
            of 2000 µs was considered. Furthermore, the sensitivity of
            the numerical simulation to the grid size and time step was
            investigated to ensure that the right mesh and time step
            has been chosen.  Figure 2b and c shows the maximum
            wall shear stress, i.e., one of the most sensitive parameters
            in relation to grid size, during the time for different grid   Figure 3. The geometrical parameters used to describe the dispensing
            sizes (course, medium, and fine) and time steps (12.5, 25,   process. H, l, and D indicate nozzle-to-platform distance, droplet lead
                                                               vertical position, and nozzle diameter, respectively.
            and 50 ns). As evident from these graphs, the variation
            of the simulation results was within an acceptable range.   Figure 4 illustrates the dispensing dynamics predicted by
            Therefore, the medium mesh and time step of 25 ns was   simulation model considering two nozzle sizes, 150 µm
            chosen for follow-up simulations and analysis.     and 300 µm, at different upstream hydrostatic pressures.
                                                               Alginate 1.5% w/v and air at 25°C were considered the
            3.3. Transition from a droplet to a jet            liquid and gas phases, respectively. The nozzle-to-platform
            Figure 3 depicts the geometrical parameters used to   distance (H) was set to 1.2 mm for both microvalves. At
            describe the dispensing dynamics of a droplet, and   low upstream pressure, i.e., 0.8 bar for the 150-µm nozzle


            Volume 9 Issue 4 (2023)                        387                         https://doi.org/10.18063/ijb.743
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