The influence of a 3D macroporous scaffold (Sponceram) on the differentiation process into bone cells was investigated under static conditions in cell culture dishes. Furthermore, cultivations were performed using a new bioreactor system in the presence or absence of bone morphogenetic protein 2 (BMP-2). Preosteoblastic MC3T3-E1 cells were first cultured on Sponceram scaffolds in 96-well dishes using standard medium, differentiation medium and BMP-2 medium. Cell proliferation showed a similar course for all conditions used. Alkaline phosphatase (AP) activity resulted in a maximum at day 5 in the presence of BMP-2. Two bioreactor cultivations were performed in a BIOSTAT Bplus RBS (rotating bed system) 500 on Sponceram carrier discs. One cultivation was performed using standard medium. The second one was used with the same medium with BMP-2 substituted. Significant calcification of the extracellular matrix in the presence of BMP-2 occurred but even in the absence of BMP-2 mineralization was observed. mRNA expression of collagen I, osteocalcin and bone sialoprotein was detected after both reactor cultivations. This study demonstrates that macroporous Sponceram is suitable for the cultivation and differentiation of MC3T3-E1 cells into the osteoblastic phenotype. The results of the bioreactor cultivation revealed that the scaffold promoted the differentiation process even in the absence of BMP-2.
The main challenge in the development of bioreactors for tissue engineering is the delivery of a sufficient nutrient and oxygen supply for cell growth in a 3D environment. Thus, a new rotating bed system bioreactor for tissue engineering applications was developed. The system consists of a culture vessel as well as an integrated rotating bed of special porous ceramic discs and a process control unit connected with the reactor to ensure optimal culturing conditions. The aim of the project was the design and construction of a fully equipped rotating bed reactor, and in particular, the characterization and optimization of the system with regard to technical parameters such as mixing time and pH-control to guarantee optimal conditions for cell growth and differentiation. Furthermore, the applicability of the developed system was demonstrated by cultivation of osteoblast precursor cells. The porous structure of the ceramic discs and the external medium circulation loop provide an optimal environment for tissue generation in long-term cultivations. Mass transfer limitations were minimized by the slow rotation, which also provides the cells with sufficient nutrients and oxygen through alternate contact to air and medium. An osteoblast precursor cell line was successfully cultivated in this bioreactor for 28 days.
The improvement of specific productivity is a continuous challenge for bioprocesses involving mammalian cells, and hence, high‐throughput methods and low‐cost strategies are needed for the selection of high producers. The aim of this study was the productivity improvement of the hybridoma cell line IV F 19.23. For this purpose, a cell surface affinity matrix assay was established to identify and select high producers. This assay is based on the binding of secreted monoclonal antibodies to an affinity matrix assembled on the outer cell membrane. A protein microarray approach was used to investigate and optimize the functionality of the affinity matrix. The protein microarray was particularly useful to identify critical steps of the staining method, such as unspecific binding, before it was applied to the hybridoma cell line. Secreting hybridomas were treated with the affinity matrix and then selected via flow‐cytometric cell sorting in four consecutive bulk sort rounds. The applied bulk strategy, allowing low screening costs, resulted in a 125% increase in specific productivity of the cell line in comparison to the initial population.
The newly developed in situ oxygen uptake rate (in situ OUR) probe presented in this article is based on the in situ microscope technology platform. It is designed to measure the oxygen uptake rate (OUR) of mammalian cells, an important parameter for metabolic flux analysis, inside a reactor (in situ) and in real-time. The system isolates a known volume of cell culture from the bulk inside the bioreactor, monitors the oxygen consumption over time, and releases the sample again. The sample is mixed during the measurement with a new agitation system to keep the cells in suspension and prevent oxygen concentration gradients. The OUR measurement system also doubles as a standard dissolved oxygen (DO) probe for process monitoring when it is not performing OUR measurements. It can be equipped with two different types of optical sensors (i.e., DO, pH) simultaneously or a conventional polarographic DO-probe (Clark type). This new probe was successfully tested in baby hamster kidney perfusion cell cultures.
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