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International Journal of Bioprinting                              Automated bioink mixer improves bioprinting



























































            Figure 5. Influence of mixing condition on cell distribution and viability. A 6% alginate hydrogel and a HEK293-GFP cell suspension were mixed by the
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            automated mixing device. The final bioink contained 3% alginate and had a cell density of 10  cells/mL. Fluorescence microscopy images show the cell
            distribution after mixing (A, C, E), and the absorbance in the XTT assays represents the metabolic activity of the cells 1 day after mixing and bioprinting
            (B, D, F). Influence of mixing speed (fixed exchange number of 100 times, referring to how many times the mixture was transferred from one syringe to
            another) (A, B), number of exchanges (fixed mixing speed of 10 mm/s) (C, D), and various combinations of mixing speed/mixing number (E, F). n = 3;
            data are expressed as mean ± SD; *p < 0.05, **p < 0.01, and ****p < 0.0001 by one-way ANOVA.

            speeds. In contrast, considerable formation of cell   clustering  was  completely  gone  at  speeds  of  30  and  50
            clusters was observed when using a lower mixing speed   mm/s. However, data from XTT assay revealed that
            of 5 mm/s, indicating uneven mixing in microscale level.   the cell viability was significantly lower at speeds of 30
            This observation was further conformed by the zigzag   and 50 mm/s (Figure 5B). In particular, a 50% decrease
            extrusion of the bioink, which contained numerous cell   in viability was detected in cells subjected to a mixing
            aggregates (Figure S1B in Supplementary File, white dots   speed of 50 mm/s, which caused severe shearing during
            indicate a strong signal reflecting high local cell density,   the process. This strong shearing can be attributed to
            which is much greater than other areas displayed in dark   the extremely high flow rate (calculated to be around
            purple). Cell distribution was substantially improved   16 times the mixing speed) in the coupler area within a
            when the mixing speed increased to 10 mm/s, and the   constrained shape (Figure 2C).


            Volume 10 Issue 2 (2024)                       388                                doi: 10.36922/ijb.1974
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