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Systematic Thermal Analysis for Accurately Predicting the Extrusion Printability
           values of these figures are 0.9744, 0.9757, and 0.9833,   3.5. Cell-laden scaffold fabrication
           respectively (P<0.001).                             In this study, printability was represented by the shape
               In addition, the 23-G nozzle was used to verify the
           physical model and to print lines with a linewidth step.   integrity and cell viability after printing. The rheological
                                                               properties of the bioinks (in Section 3.1) and the physical
           With a nozzle diameter of 340 μm, the linewidth gradient   models (in Section 3.3) provided the foundation for cell-
           of the 23-G nozzle was 340, 390, 440, 490, and 540 μm.   laden bioprinting. The effect of pressure and nozzle type
           In the first set of experiments, the pressure and velocity   had  been  explored  previously  and  had  confirmed  that
           were set at constants of 90 kPa and 8 mm/s, respectively.   higher  shear  stresses result  in  lower  cell  viability [23,27] .
           The extrudate’s theoretical  temperature  was calculated   Therefore,  the 23-G nozzle  was adapted  to investigate
           according  to  Eq.  (16)  and  was  realized  by  regulating   the influence of temperature on cell viability. Cell-laden
           the  nozzle  temperature  based  on  both  Eq.  (6)  and  the   scaffolds were fabricated at different temperatures using a
           thermal  simulation.  The  extrudate  temperature  was   bioink comprising sodium alginate–gelatin hydrogel and
           regulated  separately  at  25°C,  25.5°C,  25.9°C,  26.3°C,   HKs with a cell density of 3 × 10 /mL.
                                                                                          6
           and 26.7°C. Then, in the second set of experiments, the   Three grid patterns were printed using the cell-laden
           pressure was set sequentially at 68, 78, 90, 98, and 105   bioink; to optimize printability, the study used the 23-G
           kPa. The temperature and velocity of the extrudate were   nozzle, 130 kPa of pressure, and a velocity of 7 mm/s.
           maintained at 25.9°C and 8 mm/s. In addition, in the third   The extrudate  temperature  was regulated  separately
           set of experiments, the velocity (as a controlled variable)   at 24°C (Figures 8A-E), 27°C (Figures 8B-F), and
           was set to 13.2, 10, 8, 6.4, and 5.2 mm/s, respectively. The   30°C  (Figures  8C-G).  The  LIVE/DEAD  cell  viability
           temperature and pressure of the extrudate were maintained   assay revealed  the  cells’ viability  after  printing  to be
           as constants at 25.9°C and 90 kPa. Figures 7F-H plot the   89.21±4.09%, 91.83±2.05%, and 93.94±3.92%, as shown
           results of the three sets of experiments, and the separate   in Figure 8D.
           R-square values of these results are 0.9724, 0.9661, and   The printing results revealed that the cell viability
           0.9693, (P<0.001).                                  was almost identical in each experimental setup, although
               Lines  with  controllable  linewidths  were  printed   the  shape  fidelity  changed  significantly  according  to
           during  six  sets  of  experiments  with  a  linewidth  step   temperature.  Shape  fidelity  was  compromised  when
           of about  50  μm. The  remarkably  high  R  values  show   printing with bioink at a temperature  higher than the
                                              2
           that  the  applied  parameters  effectively  fabricated  lines   gelation  point  of  the  ink.  The  minor  change  in  cell
           with  the  expected  linewidth.  Compared  with  the  lines   viability could be due to the different lengths of time the
           printed by the 32-G nozzle, the lines printed by the 23-G   cells remained in the syringe .
                                                                                       [25]
           nozzle (with a wider ID) were more difficult to control,   The  criterion  for selecting  appropriate  printing
           which can be explained by Eq. (16). A larger diameter   parameters  using  soft  materials  was  described  in  Eq.
           nozzle requires both lower pressure and velocity to print   (16). It was confirmed by the result of the fluorescent live/
           lines, thereby exacerbating the inherent error of the 3D   dead staining that the optimized printing process had no
           bioprinter and increasing the difficulty in controlling the   significant negative impact on cell viability. Ouyang et al.
           linewidth.                                          reported a similar conclusion .
                                                                                       [27]
           A                   B                    C                   D






           E                    F                  G









           Figure 8. Cell-laden scaffolds: (A) Scaffolds printed in 24℃; (B) Scaffolds printed in 27℃; (C) Scaffolds printed in 30℃; (D) The viability
           of the cells printed in different temperature; (E) Live/dead staining images of scaffolds printed in 24℃; (F) LIVE/DEAD staining images of
           scaffolds printed in 27℃; (G) LIVE/DEAD staining images of scaffolds printed in 30℃ (n=3, P>0.05, error=S.D.).


           120                         International Journal of Bioprinting (2021)–Volume 7, Issue 3
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