Three-dimensional cell seeding and growth in radial-flow perfusion bioreactor for in vitro tissue reconstruction

Radial-flow perfusion bioreactor systems have been designed and evaluated to enable direct cell seeding into a three-dimensional (3-D) porous scaffold and subsequent cell culture for in vitro tissue reconstruction. However, one of the limitations of in vitro regeneration is the tissue necrosis that occurs at the central part of the 3-D scaffold. In the present study, tubular poly-L-lactic acid (PLLA) porous scaffolds with an optimized pore size and porosity were prepared by the lyophilization method, and the effect of different perfusion conditions on cell seeding and growth were compared with those of the conventional static culture. The medium flowed radially from the lumen toward the periphery of the tubular scaffolds. It was found that cell seeding under a radial-flow perfusion condition of 1.1 mL/cm2 x min was effective, and that the optimal flow rate for cell growth was 4.0 mL/cm2 x min. At this optimal rate, the increase in seeded cells in the perfusion culture over a period of 5 days was 7.3-fold greater than that by static culture over the same period. The perfusion cell seeding resulted in a uniform distribution of cells throughout the scaffold. Subsequently, the perfusion of medium and hence the provision of nutrients and oxygen permitted growth and maintenance of the tissue throughout the scaffold. The perfusion seeding/culture system was a much more effective strategy than the conventional system in which cells are seeded under a static condition and cultured in a bioreactor such as a spinner flask.     

Uniform tissues engineered by seeding and culturing cells in 3D scaffolds under perfusion at defined oxygen tensions

In this work, we assessed whether culture of uniformly seeded chondrocytes under direct perfusion, which supplies the cells with normoxic oxygen levels, can maintain a uniform distribution of viable cells throughout porous scaffolds several milimeters in thickness, and support the development of uniform tissue grafts. An integrated bioreactor system was first developed to streamline the steps of perfusion cell seeding of porous scaffolds and perfusion culture of the cell-seeded scaffolds. Oxygen tensions in perfused constructs were monitored by in-line oxygen sensors incorporated at the construct inlet and outlet. Adult human articular chondrocytes were perfusion-seeded into 4.5 mm thick foam scaffolds at a rate of 1 mm/s. Cell-seeded foams were then either cultured statically in dishes or further cultured under perfusion at a rate of 100 microm/s for 2 weeks. Following perfusion seeding, viable cells were uniformly distributed throughout the foams. Constructs subsequently cultured statically were highly heterogeneous, with cells and matrix concentrated at the construct periphery. In contrast, constructs cultured under perfusion were highly homogeneous, with uniform distributions of cells and matrix. Oxygen tensions of the perfused medium were maintained near normoxic levels (inlet congruent with 20%, outlet > 15%) at all times of culture. We have demonstrated that perfusion culture of cells seeded uniformly within porous scaffolds, at a flow rate maintaining a homogeneous oxygen supply, supports the development of uniform engineering tissue grafts of clinically relevant thicknesses.     

Enhancing cell seeding of scaffolds in tissue engineering through manipulation of hydrodynamic parameters

The seeding of cells onto biocompatible scaffolds is a determinant step in the attainment of functional properties of engineered tissues. Efficient, fast and spatially uniform cell seeding can improve the clinical potential of engineered tissue templates. One way to approach these cell seeding requirements is through bioreactor design. In the present study, bovine chondrocytes were seeded (2.5, 5.0 or 10.0 million cells per scaffold) onto polyglycolic acid scaffolds within the hydrodynamic environments of wavy-walled and spinner flask bioreactors. Previous characterizations of the hydrodynamic environment in the vicinity of constructs cultivated in these bioreactors suggested decreased flow-induced shear stress as well as increased recirculation and magnitude of the axial fluid velocities in the wavy-walled bioreactor. Here we report more efficient and spatially uniform cell seeding in the wavy-walled bioreactor, and at intermediate initial cell densities (5 million cells per scaffold). This study constitutes an important step towards the achievement of functional tissue-engineered implants by (i) increasing our understanding of the influence of hydrodynamic parameters on the efficiency and spatial distribution of cell attachment to scaffolds and the production of extracellular matrix and (ii) introducing a comprehensive approach to the investigation of the effects of bioprocessing conditions on tissue morphology and composition.     

接种方式对细胞在三维材料中接种率和分布的影响

考察了静态和动态接种方式对成纤维细胞在胶原壳聚糖支架材料中接种率和分布的影响。将人成纤维细胞制成细胞悬液,分别采用静态接种、转瓶接种和灌注接种方式将细胞接入三维胶原壳聚糖海绵。通过MTT法和切片HE染色分别考察细胞接种率及细胞在三维材料中的分布。实验结果表明：在低的接种密度下静态接种有较高的接种率(889%),但随着接种密度的增加接种率下降显著,细胞结团且分布不均匀;转瓶接种的接种率约为60%,细胞分布也不均匀;灌注接种的接种率始终维持在77%以上,能得到高的起始细胞密度,且细胞分布均匀,是一种理想的接种方式。细胞接种方式的优化为改善工程化组织的结构和功能、缩短体外构建时间奠定了基础。     

Flow perfusion rate modulates cell deposition onto scaffold substrate during cell seeding

The combination of perfusion bioreactors with porous scaffolds is beneficial for the transport of cells during cell seeding. Nonetheless, the fact that cells penetrate into the scaffold pores does not necessarily imply the interception of cells with scaffold substrate and cell attachment. An in vitro perfusion system was built to relate the selected flow rate with seeding efficiency. However, the in vitro model does not elucidate how the flow rate affects the transport and deposition of cells onto the scaffold. Thus, a computational model was developed mimicking in vitro conditions to identify the mechanisms that bring cells to the scaffold from suspension flow. Static and dynamic cell seeding configurations were investigated. In static seeding, cells sediment due to gravity until they encounter the first obstacle. In dynamic seeding, 12, 120 and 600 \(\upmu \hbox {l/min}\) flow rates were explored under the presence or the absence of gravity. Gravity and secondary flow were found to be key factors for cell deposition. In vitro and in silico seeding efficiencies are in the same order of magnitude and follow the same trend with the effect of fluid flow; static seeding results in higher efficiency than dynamic perfusion although irregular spatial distribution of cells was found. In dynamic seeding, 120 \(\upmu \hbox {l/min}\) provided the best seeding results. Nevertheless, the perfusion approach reports low efficiencies for the scaffold used in this study which leads to cell waste and low density of cells inside the scaffold. This study suggests gravity and secondary flow as the driving mechanisms for cell-scaffold deposition. In addition, the present in silico model can help to optimize hydrodynamic-based seeding strategies prior to experiments and enhance cell seeding efficiency.     

Improved seeding of chondrocytes into polyglycolic acid scaffolds using semi-static and alginate loading methods

Cell seeding and attachment in three-dimensional scaffolds is a key step in tissue engineering with implications for cell differentiation and tissue development. In this work, two new seeding methods were investigated using human chondrocytes and polyglycolic acid (PGA) fibrous mesh scaffolds. A simple semi-static seeding method using culture plates and tissue flasks was developed as an easy-to-perform modification of static seeding. An alginate-loading method was also studied, using alginate hydrogel as an adjuvant for entrapping cells within PGA scaffolds. Both the semi-static and PGA-alginate methods produced more homogeneous cell distributions than conventional static and dynamic seeding. Using 20 × 10(6) cells, whereas the seeding efficiency for static seeding was only 52%, all other techniques produced seeding efficiencies of ≥ 90%. With 40 × 10(6) cells, the efficiency of semi-static seeding declined to 74% while the dynamic and PGA-alginate methods retained their ability to accommodate high cell numbers. The seeded scaffolds were cultured in recirculation bioreactors to determine the effect of seeding method on cartilage production. Statically seeded scaffolds did not survive the 5-week cultivation period. Deposition of extracellular matrix in scaffolds seeded using the semi-static and PGA-alginate methods was more uniform compared with scaffolds seeded using the dynamic method. The new semi-static and PGA-alginate seeding methods developed in this work are recommended for tissue engineering because they provide substantial benefits compared with static seeding in terms of seeding efficiency, cell distribution, and cartilage deposition while remaining simple and easy to execute.     

Perfusion bioreactor system for human mesenchymal stem cell tissue engineering: dynamic cell seeding and construct development

Human mesenchymal stem cells (hMSCs) have great potential for therapeutic applications. A bioreactor system that supports long-term hMSCs growth and three-dimensional (3-D) tissue formation is an important technology for hMSC tissue engineering. A 3-D perfusion bioreactor system was designed using non-woven poly (ethylene terepthalate) (PET) fibrous matrices as scaffolds. The main features of the perfusion bioreactor system are its modular design and integrated seeding operation. Modular design of the bioreactor system allows the growth of multiple engineered tissue constructs and provides flexibility in harvesting the constructs at different time points. In this study, four chambers with three matrices in each were utilized for hMSC construct development. The dynamic depth filtration seeding operation is incorporated in the system by perfusing cell suspensions perpendicularly through the PET matrices, achieving a maximum seeding efficiency of 68%, and the operation effectively reduced the complexity of operation and the risk of contamination. Statistical analyses suggest that the cells are uniformly distributed in the matrices. After seeding, long-term construct cultivation was conducted by perfusing the media around the constructs from both sides of the matrices. Compared to the static cultures, a significantly higher cell density of 4.22 x 10(7) cell/mL was reached over a 40-day culture period. Cellular constructs at different positions in the flow chamber have statistically identical cell densities over the culture period. After expansion, the cells in the construct maintained the potential to differentiate into osteoblastic and adipogenic lineages at high cell density. The perfusion bioreactor system is amenable to multiple tissue engineered construct production, uniform tissue development, and yet is simple to operate and can be scaled up for potential clinical use. The results also demonstrate that the multi-lineage differentiation potential of hMSCs are preserved even after extensive expansion, thus indicating the potential of hMSCs for functional tissue construct development. The system has important applications in stem cell tissue engineering.     

Bioreactor improves the growth and viability of chondrocytes in the knitted poly-L,D-lactide scaffold

In the present study bovine chondrocytes were cultured in two different environments (static flasks and bioreactor) in knitted poly-L,D-lactide (PLDLA) scaffolds up to 4 weeks. Chondrocyte viability was assessed by employing cell viability fluorescence markers. The cells were visualized using confocal laser scanning microscopy and scanning electron microscopy. The mechanical properties and uronic acid contents of the scaffolds were tested. Our results showed that cultivation in a bioreactor improved the growth and viability of the chondrocytes in the PLDLA scaffolds. Cells were observed both on and in between the fibrils of scaffold. Furthermore, chondrocytes cultured in the bioreactor, regained their original round phenotypes, whereas those in the static flask culture were flattened in shape. Confocal microscopy revealed that chondrocytes from the bioreactor were attached on both sides of the scaffold and sustained viability better during the culture period. Uronic acid contents of the scaffolds, cultured in bioreactor, were significantly higher than in those cultured in static flasks for 4 weeks. In summary, our data suggests that the bioreactor is superior over the static flask culture when culturing chondrocytes in knitted PLDLA scaffold.     

培养方式对真皮组织体外构建的影响

采用静态培养和转瓶培养方式分别构建真皮组织,考察培养方式和搅拌转速对细胞在三维支架材料中增殖、代谢、分布的影响。结果表明,由转瓶培养方式构建的细胞-材料复合物,其最终细胞密度和细胞比生长速率均明显高于静态培养（14.2~27.6×106 cells/cm3 vs 10.1×106 cells/cm3和0.145~0.262 d-1 vs 0.111 d-1）,而转速达80 r/min的转瓶尤其突出;静态培养的细胞-材料复合物内部细胞稀少,且分布不均匀,转瓶培养的细胞-材料复合物在材料表面和内部细胞密度都有所提高,分布情况也得到改善,且80 r/min转瓶培养的组织其细胞密度和分布均优于10 r/min和40 r/min转瓶培养。转瓶培养在其转速达到一定强度时能明显提高细胞在支架中的增殖速率,缩短培养时间,并有效改善细胞在支架内的分布,是一种理想的培养方式。     

Effects of filtration seeding on cell density, spatial distribution, and proliferation in nonwoven fibrous matrices

The cell seeding density and spatial distribution in a 3-D scaffold are critical to the morphogenetic development of an engineered tissue. A dynamic depth-filtration seeding method was developed to improve the initial cell seeding density and spatial distribution in 3-D nonwoven fibrous matrices commonly used as tissue scaffolds. In this work, trophoblast-like ED27 cells were seeded in poly(ethylene terephthalate) (PET) matrices with various porosities (0.85-0.93). The effects of the initial concentration of cells in the suspension used to seed the PET matrix and the pore size of the matrix on the resulting seeding density and subsequent cell proliferation and tissue development were studied. Compared to the conventional static seeding method, the dynamic depth-filtration seeding method gave a significantly higher initial seeding density (2-4 x 10(7) vs 4 x 10(6) cells/cm3), more uniform cell distribution, and a higher final cell density in the tissue scaffold. The more uniform initial cell spatial distribution from the filtration seeding method also led to more cells in S phase and a prolonged proliferation period. However, both uniform spatial cell distribution and the pore size of the matrices are important to cell proliferation and morphological development in the seeded tissue scaffold. Large-pore matrices led to the formation of cell aggregates and thus might reduce cell proliferation. The dynamic depth-filtration seeding method is better in providing a higher initial seeding density and more uniform cell distribution and is easier to apply to large tissue scaffolds. A depth-filtration model was also developed and can be used to simulate the seeding process and to predict the maximum initial seeding densities in matrices with different porosities.     

Distribution of bone-marrow stromal cells in a 3D scaffold depending on the seeding method and the scaffold inside a surface modification

The distribution of bone-marrow stromal cells (BMSC) was studied in 3D polylactide scaffolds. Seeding of cells into the scaffold by the dynamic method (with the aid of a peristaltic pump) has been shown to provide distribution of cells throughout the entire scaffold volume, unlike the static method of seeding, in which the cell suspension is applied onto the scaffold surface. Unlike the cells seeded into the scaffold by the dynamic method, the cells seeded by the static method practically completely migrate from the scaffold on the dish for the first several days. It is revealed that BMSCs cultivated in 3D polylactide scaffolds modified by fibrin form colonies, whereas BMSCs cultivated inside scaffolds modified by collagen type 1 distribute all over the scaffold volume in the form of individual cells.     

Comparisons of microcarrier cell culture processes in one hundred mini-liter spinner flask and fifteen-liter bioreactor cultures

Microcarrier cell culture process can be used to culture anchorange-dependent cells in large bioreactor vessels. The process performance in large bioreactors is usually less prominent than that in spinner flask vessels and bench scale reactors. In this study we investigated the microcarrier cell culture processes in 100?ml spinner flask and 15-liter bioreactor cultures, including the kinetics for cell attachment, cell growth and the production of Japanese encephaltilis vaccine strain (Beijing-1) virus. Under a fixed concentration of microcarrier and cell density used in inoculations, the attachment kinetics of Vero cells on Cytodex 1 microcarrier in a 15-liter bioreactor vessel was 2 folds slower than with 100?ml spinner flask culture. Virus replication in 15-liter bioreactor culture also revealed an approximately one day lag-time compared to 100?ml spinner flask culture. Findings presented herein provide valuable information for designing and operating microcarrier cell culture processes in large bioreactor vessels.     

In silico multi‐scale model of transport and dynamic seeding in a bone tissue engineering perfusion bioreactor

Computer simulations can potentially be used to design, predict, and inform properties for tissue engineering perfusion bioreactors. In this work, we investigate the flow properties that result from a particular poly‐L ‐lactide porous scaffold and a particular choice of perfusion bioreactor vessel design used in bone tissue engineering. We also propose a model to investigate the dynamic seeding properties such as the homogeneity (or lack of) of the cellular distribution within the scaffold of the perfusion bioreactor: a pre‐requisite for the subsequent successful uniform growth of a viable bone tissue engineered construct. Flows inside geometrically complex scaffolds have been investigated previously and results shown at these pore scales. Here, it is our aim to show accurately that through the use of modern high performance computers that the bioreactor device scale that encloses a scaffold can affect the flows and stresses within the pores throughout the scaffold which has implications for bioreactor design, control, and use. Central to this work is that the boundary conditions are derived from micro computed tomography scans of both a device chamber and scaffold in order to avoid generalizations and uncertainties. Dynamic seeding methods have also been shown to provide certain advantages over static seeding methods. We propose here a novel coupled model for dynamic seeding accounting for flow, species mass transport and cell advection‐diffusion‐attachment tuned for bone tissue engineering. The model highlights the timescale differences between different species suggesting that traditional homogeneous porous flow models of transport must be applied with caution to perfusion bioreactors. Our in silico data illustrate the extent to which these experiments have the potential to contribute to future design and development of large‐scale bioreactors. Biotechnol. Bioeng. 2013; 110: 1221–1230. © 2012 Wiley Periodicals, Inc.     

Design and validation of a dynamic flow perfusion bioreactor for use with compliant tissue engineering scaffolds

In tissue engineering, flow perfusion bioreactors can be used to enhance nutrient diffusion while mechanically stimulating cells to increase matrix production. The goal of this study was to design and validate a dynamic flow perfusion bioreactor for use with compliant scaffolds. Using a non-permanent staining technique, scaffold perfusion was verified for flow rates of 0.1-2.0 mL/min. Flow analysis revealed that steady, pulsatile and oscillatory flow profiles were effectively transferred from the pump to the scaffold. Compared to static culture, bioreactor culture of osteoblast-seeded collagen-GAG scaffolds led to a 27-34% decrease in cell number but stimulated an 800-1200% increase in the production of prostaglandin E(2), an early-stage bone formation marker. This validated flow perfusion bioreactor provides the basis for optimisation of bioreactor culture in tissue engineering applications.     

3D culture of osteoblast‐like cells by unidirectional or oscillatory flow for bone tissue engineering

A medium perfusion system is expected to be beneficial for three‐dimensional (3D) culture of engineered bone, not only by chemotransport enhancement but also by mechanical stimulation. In this study, perfusion systems with either unidirectional or oscillatory medium flow were developed, and the effects of the different flow profiles on 3D culturing of engineered bone were studied. Mouse osteoblast‐like MC 3T3‐E1 cells were 3D‐cultured with porous ceramic scaffolds in vitro for 6 days under static and hydrodynamic conditions with either a unidirectional or oscillatory flow. We found that, in the static culture, the cells proliferated only on the scaffold surfaces. In perfusion culture with the unidirectional flow, the proliferation was significantly higher than in the other groups but was very inhomogeneous, which made the construct unsuitable for transplantation. Only the oscillatory flow allowed osteogenic cells to proliferate uniformly throughout the scaffolds, and also increased the activity of alkaline phosphatase (ALP). These results suggested that oscillatory flow might be better than unidirectional flow for 3D construction of cell‐seeded artificial bone. The oscillatory perfusion system could be a compact, safe, and efficient bioreactor for bone tissue engineering. Biotechnol. Bioeng. 2009;102: 1670–1678. © 2008 Wiley Periodicals, Inc.     

Optimization of cardiac cell seeding and distribution in 3D porous alginate scaffolds

Cardiac tissue engineering has evolved as a potential therapeutic approach to assist in cardiac regeneration. We have recently shown that tissue-engineered cardiac graft, constructed from cardiomyocytes seeded within an alginate scaffold, is capable of preventing the deterioration in cardiac function after myocardial infarction in rats. The present article addresses cell seeding within porous alginate scaffolds in an attempt to achieve 3D high-density cardiac constructs with a uniform cell distribution. Due to the hydrophilic nature of the alginate scaffold, its >90% porosity and interconnected pore structure, cell seeding onto the scaffold was efficient and short, up to 30 min. Application of a moderate centrifugal force during cell seeding resulted in a uniform cell distribution throughout the alginate scaffolds, consequently enabling the loading of a large number of cells onto the 3D scaffolds. The percent cell yield in the alginate scaffolds ranged between 60-90%, depending on cell density at seeding; it was 90% at seeding densities of up to 1 x 10(8) cells/cm(3) scaffold and decreased to 60% at higher densities. The highly dense cardiac constructs maintained high metabolic activity in culture. Scanning electron microscopy revealed that the cells aggregated within the scaffold pores. Some of the aggregates were contracting spontaneously within the matrix pores. Throughout the culture there was no indication of cardiomyocyte proliferation within the scaffolds, nor was it found in 3D cultures of cardiofibroblasts. This may enable the development of cardiac cocultures, without domination of cardiofibroblasts with time.     

The dynamics of surface acoustic wave‐driven scaffold cell seeding

Flow visualization using fluorescent microparticles and cell viability investigations are carried out to examine the mechanisms by which cells are seeded into scaffolds driven by surface acoustic waves. The former consists of observing both the external flow prior to the entry of the suspension into the scaffold and the internal flow within the scaffold pores. The latter involves micro‐CT (computed tomography) scans of the particle distributions within the seeded scaffolds and visual and quantitative methods to examine the morphology and proliferation ability of the irradiated cells. The results of these investigations elucidate the mechanisms by which particles are seeded, and hence provide valuable information that form the basis for optimizing this recently discovered method for rapid, efficient, and uniform scaffold cell seeding. Yeast cells are observed to maintain their size and morphology as well as their proliferation ability over 14 days after they are irradiated. The mammalian primary osteoblast cells tested also show little difference in their viability when exposed to the surface acoustic wave irradiation compared to a control set. Together, these provide initial feasibility results that demonstrate the surface acoustic wave technology as a viable seeding method without risk of denaturing the cells. Biotechnol. Bioeng. 2009;103: 387–401. © 2009 Wiley Periodicals, Inc.     

Bead-to-bead transfer of chinese hamster ovary cells using macroporous microcarriers

Chinese hamster ovary cells (CHO-K1) were cultivated in macroporous gelatin microcarriers (CultiSpher G and CultiSpher S) in spinner flasks and a 5 1 bioreactor. Near-to-confluent cultures were harvested by bead-to-bead transfer where intact microcarriers with cells were transferred from a spinner flask to another spinner flask or to the bioreactor with naked microcarrier beads. Successful bead-to-bead transfer was achieved in various split ratios. The duration of attachment seemed to be important where the direct contact of beads to each other can be achieved by intermittent stirring. Repeated transfers were performed and at least four transfers in spinner flasks were achieved.Two variations of bead-to-bead transfer were performed in the 5 1 bioreactor either by seeding the bioreactor with near-to-confluent beads cultivated in spinner flasks orin situ transfer by adding fresh beads to the bioreactor. As in the spinner case, attachment was achieved by intermittent stirring where donor beads were in close proximity to the acceptor beads. Again successful transfers were obtained as evidenced by the good growth on acceptor beads where cell yields were in the range of 3100–4500 cells/bead.The results suggest that bead-to-bead transfer of CHO-K1 cells can be easily performed and do provide an alternative route to applications where dissolution techniques may not offer an efficient solution.     

Flow cytometric cell cycle analysis of muscle precursor cells cultured within 3D scaffolds in a perfusion bioreactor

It has been widely demonstrated that perfusion bioreactors improve in vitro three‐dimensional (3D) cultures in terms of high cell density and uniformity of cell distribution; however, the studies reported in literature were primarily based on qualitative analysis (histology, immunofluorescent staining) or on quantitative data averaged on the whole population (DNA assay, PCR). Studies on the behavior, in terms of cell cycle, of a cell population growing in 3D scaffolds in static or dynamic conditions are still absent. In this work, a perfusion bioreactor suitable to culture C₂C₁₂ muscle precursor cells within 3D porous collagen scaffolds was designed and developed and a method based on flowcytometric analyses for analyzing the cell cycle in the cell population was established. Cells were extracted by enzymatic digestion of the collagen scaffolds after 4, 7, and 10 days of culture, and flow cytometric live/dead and cell cycle analyses were performed with Propidium Iodide. A live/dead assay was used for validating the method for cell extraction and staining. Moreover, to investigate spatial heterogeneity of the cell population under perfusion conditions, two stacked scaffolds in the 3D domain, of which only the upstream layer was seeded, were analyzed separately. All results were compared with those obtained from static 3D cultures. The live/dead assay revealed the presence of less than 20% of dead cells, which did not affect the cell cycle analysis. Cell cycle analyses highlighted the increment of cell fractions in proliferating phases (S/G₂/M) owing to medium perfusion in long‐term cultures. After 7–10 days, the percentage of proliferating cells was 8–12% for dynamic cultures and 3–5% for the static controls. A higher fraction of proliferating cells was detected in the downstream scaffold. From a general perspective, this method provided data with a small standard deviation and detected the differences between static and dynamic cultures and between upper and lower scaffolds. Our methodology can be extended to other cell types to investigate the influence of 3D culture conditions on the expression of other relevant cell markers. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009