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               836                                                                                  Tissue Engineering

















                      FIGURE 14 Two common types of hollow-fiber bioreactors. In the reactor shown on the left, cells may be placed
                      either in the shell (gray color) or intrafiber space. In the reactor shown on the right, cells are typically placed in the
                      shell space.

               the viability and function of the cells, while the patient’s  impellers, which have been shown to cause significant cell
               plasma would flow on the shell side. Such a configuration  damage in other types of bioreactors. Interestingly, data
               has been described for the construction of a bioartificial  gathered on recent space missions do suggest that cells
               liver using adult hepatocytes.                    and tissues cultured in this bioreactor develop and grow
                                                                 as they would in low-gravity environments.
                 c. Rotating vessel wall bioreactor. The rotating  Over 50 types of cells, tissue constructs, and even tis-
               wall vessel bioreactor, a relatively new type of bioreac-  sueexplantshavebeenculturedinthesebioreactors,which
               tor system used in biotechnology, was originally devel-  appear to be ideally suited to promote the expression of
               oped and patented by the U.S. National Aeronautic Space  tissue-specific functions in the cultured cells and preserve
               Agency (NASA) to study the behavior of cells and tis-  the three-dimensional morphological characteristicsofthe
               sues under conditions simulating low gravity on Earth.  native tissue. Thus, this system should be useful to create
               This bioreactor consists of a chamber entirely filled with  and maintain bioartificial tissues to be subsequently im-
               culture medium containing the cells, tissue constructs, or  planted in vivo. On the other hand, these devices would
               even actual tissue explants in suspension. The chamber is  not be appropriate for tissue engineering applications re-
               rotated on a horizontal axis at a speed that approximately  quiring a combination of very high cell densities and very
               matches the terminal settling velocity of the cells or tis-  low liquid hold-up volumes, such as in the case of extra-
               sues in suspension such that they establish a fluid orbit  corporeal bioartificial livers.
               (Fig. 15). The cells or tissues therefore never hit the bot-
               tom of the reactor or touch any of its inner surfaces. An
               important feature of this system is that oxygen is deliv-  D. Morphogenesis of Engineered Tissues
               ered via gas-permeable silicone membranes; no sparging  The quantitative difference between cell–substrate and
               of gas is necessary. The design ensures uniform hydrody-  cell–cell adhesion strength on a rigid surface dramatically
               namic conditions within the bioreactor without the use of  affects the organization of cells on the substrate. A thermo-
                                                                 dynamic view of the problem suggests that the overall sys-
                                                                 tem (consisting of the cells and the extracellular support)
                                                                 ultimately reaches an equilibrium state when the surface
                                                                 free energy is minimized. According to this concept, the
                                                                 existence of large cell–substrate adhesion forces relative
                                                                 to cell–cell adhesion forces prevents cell–cell overlapping
                                                                 (Fig. 16). In contrast, the opposite situation would lead to
                                                                 cell clumping or multilayered growth on the substrate.
                                                                 This prediction is in agreement with the observation of
                                                                 cellular aggregate formation when hepatocytes are plated
                                                                 on a nonadherent surface as opposed to a highly adherent
                                                                 surface such as type I collagen.
               FIGURE 15 Design of a rotating wall vessel bioreactor. Cells are
                                                                   Heterotypic cell systems or “co-culture” systems have
               suspended in medium, which fills the vessel until no air bubble
                                                                 been used for the production of skin grafts, in long-term
               is left. Oxygen is delivered via a silicone membrane in the cen-
                                                                 culturesofhepatocytes,andinlong-termculturesofmixed
               ter of the vessel. The vessel rotates at a relatively low speed
               (∼30 rotations/min) to prevent settling of cells.  bone marrow cells. These systems take advantage of the
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