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3.1.3 Irradiation
Three types of irradiations can be used to trigger free radical production [54]. First
is single photoemission, in which a single high-energy photon is used. Second is the
two or multiple emission approaches, in which several low-energy photons are
responsible for creating the free radicals [55, 56]. Third is infrared, which is the
common source in the last two methods, although both UV and visible light can be
used in the rst method [54].
Photons can be irradiated to the initiators through two main techniques: digital
light processing (DLP) and direct laser bioprinting [57]. In DLP, a digital micromirror device (DMD) consisting of a group of mirrors reects the photons in a prespecied manner [58]. The irradiation pattern denes the orientation of the mirrors.
This approach is used in almost all SLA bioprinting systems [44]. Both visible light
and UV are used in this system.
Two-photon emission approach is used in conjunction with the direct laser writing
bioprinting system. On the contrary to the single-photon method, the material is crosslinked in the bulk volume rather than in a layer-by-layer manner. A laser beam is used
for the excitation of the photoinitiators. The intensity of the irradiation is adjusted by
altering the width modulation. Thus, it is feasible to use infrared wavelengths for
crosslinking hydrogels absorbing UV light [59]. This approach does not have a signicant impact on cell viability. Indeed, cells are more sensitive to chemical reactions,
not the laser beam [60]. Although the two-photon emission approach increases the
pace of crosslinking procedure, it requires more expensive apparatus than DLP [44].
4 Inkjet Bioprinting
4.1 Thermal Inkjet Bioprinting
Inkjet printing is categorized into continuous and drop-on-demand methods.
Thermal inkjet printing which is one of the methods related to the second category
has been widely used for bioprinting [61]. The short-lasting applied heat can only
increase the temperature by 4–10°C for a few microseconds [62]. Besides, extrusion stress can also impact cell viability, as seen in extrusion-based bioprinting [63].
The stress increases, especially in the case of using narrow nozzles.
4.2 Piezoelectric Inkjet Bioprinting
Piezoelectric inkjet printing is not recommended to be used for bio-fabrication since
the applied sonication may harm cell membrane and lead to cell lysis [62]. However,
the successful application of piezoelectric inkjet printing has been reported [64, 65].
It has been tried to decrease the stress applied to the cells by altering the amplitude
and increasing the printing time [66]. However, no correlation between survival rate
and the factors mentioned above has been reported. Meanwhile, cell agglomeration
and sedimentation signicantly impact cell survival [67]. In addition to the

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mentioned factors, low droplet directionality, nonuniform droplets, and frequent
nozzle clogging are the other drawbacks of piezoelectric inkjet bioprinting [68, 69].
To overcome the issues of piezoelectric method, acoustic inkjet printers can be
used in which the application of heat and pressure is eliminated and more uniform
droplets are formed [68, 70]. Besides, an open-pooled nozzle scan used in acoustic
systems decreases the shear stress applied to the cells during extrusion [1].
4.3 Advantages andDisadvantages
Considering that the number of cells in each droplet can be specied in this method,
it is pragmatic to consider inkjet bioprinting for quantitative cell seeding procedures. Compared to the piezoelectric approach, more technical modications can be
applied in thermal inkjet printing. Low cost, availability, and high printing speed are
the other advantages of thermal inkjet printing [68].
Droplet drying is one of the drawbacks of inkjet printing. Considering that there
is a possibility of blotting, mixing, and diffusion of the bio-ink in this procedure,
materials with gelation ability such as sodium alginate have been used in the electrostatic inkjet printing to avoid the mentioned incidents [68]. Although using
hydrogels may complicate the scaffold manipulation, direct printing of the product
on the defect can solve this problem [71]. This method has been used for cartilage
and skin regeneration [1].
Low cell concentrations are usually used in inkjet bioprinting to avoid nozzle
clogging, facilitate droplet formation, and decrease shear stress. On the other hand,
high cell concentration can impact the crosslinking procedure [71].
5 Comparison ofBioprinting Methods
Based on a study performed by Murphy etal. [1], the following points can be mentioned to compare bioprinting technologies (Fig.3): Bio-ink prepared for the laserbased bioprinting must have a higher viscosity compared to the other methods.
Viscosity
SLA>EB>IJ IJ>SLA>EB SLA>EB>IJ SLA>IJ>EB
Fig. 3 Comparison of the bioprinting technologies
Printing
Speed
Bioprinting
technologies
Printing
Resolution
Cell viability Crosslinking
EB: Thermal,
Chemical,
Photo
Chemical and
IJ and SLA:
Photo

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Besides, chemical, thermal, and photocrosslinking can be used in the extrusionbased method. However, thermal crosslinking has not been applied in laser-based
and inkjet bioprinting. Inkjet printing has the highest printing speed, and extrusionbased has the lowest. Laser-based is the optimal choice regarding the printing resolution, while inkjet printing has the lowest resolution. The rate of cell death is the
highest in extrusion-based and lowest in laser-based. Concerning the crosslinking
method, chemical, thermal, and photocrosslinking can be used in extrusion-based,
while thermal crosslinking is not used in laser-based and inkjet bioprinting.
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S. Mohaghegh and H. Nokhbatolfoghahaei

Application ofBioreactors inOral
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andMaxillofacial Surgery
HeliaSadatHaeriBoroojeni
andHaniehNokhbatolfoghahaei
1 Introduction
Bone tissue engineering (BTE) strategies include numerous manipulative measures
for the reconstruction of bone defects, using cell-laden, hierarchically organized,
and anatomical and functional tissue fragments, highly resembling the natural
inherent characteristics of bone tissue [1, 2]. However, the current methodology has
not always resulted in optimal generation of a 100% physiologic environment with
competent immune, nervous, and hormonal systems, necessary for development of
functional tissues and organs [3–5]. A major shortcoming is associated with relatively time-consuming and compromised vascularization capacities. This results in
prolonged vascularization periods and, so, compromised regenerative outcomes.
Given that oxygen diffusion takes place at approximately 200μm, cells located at
the core of implanted constructs can go through hypoxic conditions during these
periods. These conditions can contribute to representation of an altered metabolism
and eventually cell death in some cases. Scientic consensus and methodical evidence have indicated that dynamicity can promote biological systems and functional tissue engineering [6–8]. Therefore, dynamic systems have been designed
with the aim of mimicking the specics of micro- and macro-tissue environments
and reproduction of their mechanical and physiological features [8–10]. The same
tactic has been implied for bone tissue engineering. Bone tissues are under sporadic
pressure. The skeletal function encompasses bearing body loads in accordance with
the body weight and physical activities that are performed throughout the daily life.
H. S. H. Boroojeni
Department of Oral and Maxillofacial Surgery, School of Dentistry, Shahid Beheshti
University of Medical Sciences, Tehran, Iran
H. Nokhbatolfoghahaei (*)
Dental Research Center, Research Institute of Dental Sciences, Shahid Beheshti University of
Medical Sciences, Tehran, Iran
© The Author(s), under exclusive license to Springer Nature Singapore Pte Ltd. 2023
A. Khojasteh et al. (eds.), Emerging Technologies in Oral and Maxillofacial
Surgery, https://doi.org/10.1007/978-981-19-8602-4_18
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These functions are translated as a natural dynamicity that involves the skeletal
architecture of the body and cause consecutive deformation of extracellular matrix
(ECM) and lacuna-canalicular uid ow [7, 8, 11, 12]. Bony cells being highly
mechanosensitive can sense the hydrostatic pressure directly [7]. The application of
ow-induced interstitial shear stress has revealed the occurrence of a sequential
sensing procedure consisted of active direction of cellular differentiation and activation of bone remodeling series of extracellular signaling pathways (i.e., ERK1/2,
Wnt, bone morphogenetic protein (BMP)) [13]. These observations bring further
notice to the stimulating impact of mechanical encounter upon invivo bone regeneration processes [14–21].
Although static cultural settings are deprived of the pivotal impact of mechanical
stimulation, majority of invitro investigations have been designed and conducted in
a static manner [7, 8]. Static culture conditions impose hurdles upon tissue development, consequent to their compromised delivery of adequate substances and waste
removal. According to the literature, maximum diffusion distance for biotic substances is below the range of 100–200μm [7, 8]. Therefore, cells, placed at the
scaffold core, bear lower chances of survival, especially when cultured statically.
Moreover, static culturing conditions contribute to the cellular tendency for surface
attachment instead of even cellular diffusion throughout the structure [8].
Two types of mechanical stimuli have been revealed to induce cellular osteogenic differentiation: (a) uid shear stress following the movement of interstitial
uid through the lacunae during load bearing and (b) strain resulted from deformation, after occurrence of bending and compression with physical activity [8, 11, 22].
Mechanical stimuli allow culture medium streaming within scaffolds, further
contributing to the role of dynamicity in tissue engineering. Hence, restricted
expression of osteogenic markers, inhibited stem cell differentiation, and limited
nutrient diffusion to the scaffold core are among the drawbacks of static cultural
settings that inherently tend to disregard the role of dynamicity in tissue generation
and growth. Constraints of static culturing have led to an ongoing endeavors for
incorporating mechanical stimuli [6, 23], using bioreactors. Bioreactors are housing
devices that provide controlled conditions that allow enactment of physiologic, biologic, and biochemical phenomena within articial tissue constructs. Initial objective of bioreactors was to test biomaterials, but afterward, various modalities were
developed aiming for extracorporeal tissue growth. Incorporation of bioreactors in
terms of tissue engineering has led to the recent emergence of the term “Tissue
Engineering Quadriad” as for the combination of cells, carrier constructs, signaling
factors, and bioreactor systems, which formerly only consisted of rst three components, the so-called tissue engineering triad [6]. Bioreactors have helped with
addressing the static culturing-associated limitations and culminated in a paradigm
shift regarding extracorporeal fabrication of viable tissue fragments. Osteogenicbased bioreactors are designed to promote osteogenic capabilities of bio-scaffolds
and “in vitro bone tissue morphogenesis,” namely, the generation of bone-like structures and ECM [24]. Bioreactors are used for facilitation, monitoring, and controlling the inherent biological or biochemical phenomena that occur within natural
tissue. Complex bioreactors allow tuning of certain physiologic parameters,

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Spinner Flask
Bioreactors
for
Bone Tissue
Engineering
In Vitro Bioreactors
In Vivo Bioreactors
Hydrodynamic-Based
Shear-Loading
Compression (Direct
Mechanical Stress)
EMF-Based
Combined
Flap Techniques
Vascular Techniques
Rotating
Perfusion-Based
Subcutaneous Pocket
Muscular Flap
Periosteal Flap
Axial Vascular Bundle (AVB)
Arteriovenous Loop (AV-Loop)
Fig. 1 Bioreactors for bone tissue engineering
including the temperature, pH, different substance concentrations, and diverse set of
stimuli, when growth modulation is yearned for [25]. Incorporated devices in a
bioreactor system are made of biologically and chemically inert materials so that
undesired reactions are primarily prohibited in the internal humidied milieu [26].
Bioreactors are known to possess the following criteria: (1) distribute cells evenly;
(2) sustain cellular requisites; (3) mix the culture mediums to emend substance diffusion and convection; (4) provide physical stimuli; and (5) provide requisites for
reproducibility, control, monitoring, and automation [27]. In vitro bioreactors helped
dened recapitulation of in vivo microenvironments within an ex vivo setting.
However, invitro developed tissues have showed lack of inherent vascular and neural
networks. This has made tissue fragments chiey reliant upon the ingrowth of neovascular sprouts of the recipient beds of host. Therefore, the principle of invivo
bioreactor (IVB) has developed to address such shortcomings (Fig.1).
2 Bioreactors forBone Tissue Engineering
Various bioreactor modalities have been designed to give a desired combination of
stimulation specics. Theoretical concepts can help the designing and fabrication of
bioreactors. For instance, mathematical modelling allows calculation of scaffold

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uid ow rates, diffusion of oxygen, implied forces, and other variables [28],
through providing insights for culturing bulk materials.
Based upon their design, bioreactors are categorized in three groups: (a) those
that are designed based on implication of hydrodynamic shear stresses, (b) those
that are designed based on implication of direct mechanical stresses, and (c) those
that are designed based on implication of electromagnetic elds (EMF) [8, 29].
H. S. H. Boroojeni and H. Nokhbatolfoghahaei
2.1 Hydrodynamic-Based Shear-Loading Bioreactors
One of simplest and most pervasive bioreactor designs is attained with hydrodynamic shear stress. The hydrodynamic shear stress is applied through medium uid
circulation. Shear-loading devices include spinner ask, rotating, and perfusionbased bioreactors [29].
2.1.1 Spinner Flask Bioreactors
The spinner ask bioreactors create a turbulent ow leading to a promoted diffusion
of biotic substances [29]. These bioreactors are relatively simple and inexpensive
systems. Spinner asks consisted of a glass reservoir, side arms, and porous ltering
covers. The reservoir holds the media, and the side arms are unlocked to reach the
reservoir’s internal space. While scaffolds are attached to the lid of unit ask with
needles, an assembled mixer starts convective forces and medium ow at the ask
center unit. Mixer’s stirring speed is set based on the aimed for shear stress that is to
be applied on scaffolds. The porous ltering covers allow the gas by-products to
exchange within the system. Once prepared, the whole ask is retained in incubators with pre-controlled temperature and oxygen-delivery content [6, 23, 30].
Spinner ask bioreactors were primarily designed to be used in BTE [31].
Spinner ask systems have been known as facile and low-cost setups, capable of
promoting proliferation and differentiation of cultured cells [6, 29, 31, 32]. They are
capable of more efciently enhancing nutrient mass transport when compared to
rotating wall vessels [6, 29]. Moreover, spinner asks can impart higher stress values upon cells. Spinner ask bioreactors can house multiple small scaffolds and
culture clinically relevant engineered tissue fragments concomitantly. This can put
spinner ask bioreactor at use when reconstruction of segmental skeletal defects is
planned [6]. With regard to development of thin bone substitutes that are used as
bone patches in restorative interventions or at bone reconstructions, spinner asks
and rotating wall vessels are both rational choices [6]. In addition to their differential and proliferative impacts, spinner ask systems have the advantage of low
acquisition costs [29].
Being hydrodynamically capable of implying shear stress, spinner ask bioreactors have improved nutrient transfer into scaffolds. However, many constraints are
still present with them. For instance, stirring action of mixers can cause a turbulent
environment within the media. This bears the probability to dissociate the attached
cells. Spinner asks’ abilities are limited in terms of mass transport and application
of desired levels of stress upon cells. An impaired systemic seal is associated with

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359
them that averts sufcient control over the O2/CO2 content of asks. There has also
remained a need for constant obligatory replacement of cultural media. Of note,
when cultivating combined cell-scaffold structures, it is likely to witness a dense
supercial cell layer. This layer can impede the biotic supply of core-retained cells
in such bioreactors. Moreover, the gradient set of convective forces in ask result in
heterogeneous application of shear stress. Concerns are present with their potential
in supporting of functional bone maturation [29, 31, 33] (Fig.2).
2.1.2 Rotating Bioreactors (Rotating Wall Vessel (RWV))
The rationale behind the design of rotating bioreactors is to use microgravity to
form three-dimensional cell clusters [23]. Rotating bioreactors imply low shear
stresses and thus promote nutrient transfer [29]. The rotating vessels of system produce shear stresses by initiating laminar ow in a horizontal axis [29]. The produced
shear stresses, despite being low in degree, contribute to the diffusion of nutrients
and waste products [29]. In preliminary models of rotating bioreactor, scaffolds
were left to oat within the media [29], resulting in collision of constructs with
Fig. 2 Spinner ask
bioreactor
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