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Feng F, et al.
           by  injecting  3%  alginate  solution  (high  viscosity)  and   A          C
           1% alginate solution (low viscosity) into the microfluidic
           printhead  simultaneously  (Figure  3).  It  was  found  that
           the ink viscosity significantly affected the flow pattern in   B           D
           the microfluidic channel and further changed the spatial
           distribution of different bioinks in the printed filament.
           When two kinds of solutions were initially injected into
           the printhead at the same flow rate, only a small proportion
           of  low-viscous  ink  flowed  into  the  outlet  channel  and
           gradually  diffused into the high-viscous side along the
           flow  direction forming a slanted interface (Figure 3C).
           When the two inks were extruded out from the nozzle,
           low-viscous ink was found to fully cover the surface of
           high-viscous  inks  (Figure  3D).    Parallel  heterogeneous   Figure 3. Flow pattern and printed filaments of alginate solution
           filaments were not clearly formed even when the flow rate   with different viscosities. (A) Injecting 3% alginate solution (high
           of low-viscous solution gradually increased (Figure S2A,   viscosity) simultaneously and (B) printed heterogeneous filaments.
           B, C, D). This implied that the presented multicomponent   (C) Injecting 3% alginate solution and 1% alginate solution and
                                                               (D) printed filaments. Scale bars are 200 µm and 1 mm.
           bioprinting is applicable to the inks with similar viscosity.
           The previous studies indicated that when the fluids have
           various  viscosities,  multiphase  flow  (liquid-liquid  two   the  representative  distribution  of  fluorescent  particles
           phase) occurs [26-31] . Since most of the bioinks are miscible   within different heights ranging from 65 µm to 585 µm
           fluid and surface tension, diffusivity at the interface is an   with  spacing  of  130  µm,  which  related  to  the  layers
           important factor to regulate the flow pattern .     consisted  of  different  ink  proportion.  To  quantitatively
                                               [32]
           3.2 Printing of Constructs With Graded              evaluate the spatial distribution of fluorescent particles,
                                                               the number of green and red fluorescent particles within
           Component Composition                               these specific heights was counted as shown in Figure 5H.
           Figure  4A  demonstrated  a  2D  filament  pattern  with   It indicates that the ratio of green and red particles was
           gradually changed ink proportion by continuously    approximately  equal  to  the  ratio  of  flow  rate  of  two
           varying the flow rate ratio of two color-coded inks from   kinds  of  inks  within  the  printhead,  which  can  finally
           2:1 to 0:1 during printing. A grid pattern with five layers   achieve the spatial gradient distribution of the particles as
           was  printed  with  continuous  changed  composition  as   designed. The unique advantage of this method is that it
           shown  in  Figure  4B.  For  each  layer,  the  color  of  the   can generate multicellular constructs with spatiotemporal
           printed filaments gradually changed from black to white   cell positioning in a controllable manner. These kinds of
           through  dynamically  adjusting  the  flow  rate  of  each   heterogeneous constructs have the potential to meet the
           inlet. Figure 4C schematically illustrates the printing of   demand of biological scaffold involving different kinds
           a multilayered construct with serials of color coding. By   of matrix. Together these results demonstrated the unique
           sequentially printing two kinds of colored inks with five   ability to continuously print heterogeneous construct in
           different flow rate ratios, a vertically gradient structure   both horizontal and altitude direction without interrupt,
           with 10 layers was finally printed and color of the specific   which  could  be  an  efficient  and  promising  method  to
           layer was gradually changed from yellow to green and   create constructs with different properties and functions.
           finally to blue as shown in Figure 4D, E, F, G, H.    Although  the  switching  process  among  different
             The  microfluidic  printhead  can  also  be  potentially   printheads  is  avoided  using  microfluidic  printhead,  the
           used  to  fabricate  gradient  multicellular  3D  constructs.   transition time to change the proportion of the inks exists
           As a proof of concept, fluorescent microparticles with a   during the printing process, which means when changing
           similar size to living cells were used to demonstrate the   the flow rates through the syringes, the proportion of inks
           feasibility.  As  schematically  shown  in  Figure  5A, the   in the printhead cannot be switched simultaneously. It was
           concentration  of  green  fluorescent  particles  gradually   found that both flow rate and the concentration influence
           decreased while that of red fluorescent particles increased   the transition time (Figure S3 and S4). For inks of alginate
           from the bottom layer to the top layer by dynamically   solution with concentration ranging from 1% to 3%, all of
           changing the flow rate ratio of two kinds of inks from 1:0 to   their transition time decreased with the increase of the
           0:1 during printing. Figure 5B illustrates the actual spatial   flow rate. However, there existed a great drop for the 3%
           distribution of green and red fluorescent particles within   alginate solution, whose transition time was about 430 s
           the printed grid hydrogel structure, which are accordant   at the flow rate of 100 µL/h and about 50 s at the flow rate
           with the predefined situation. Figure 5C, D, E, F, G shows   of 1000 µL/h. For the 1% alginate solution, the transition

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