Operation of a Benchtop Bioreactor

Fermentation systems are used to provide an optimal growth environment for many different types of cell cultures. The ability afforded by fermentors to carefully control temperature, pH, and dissolved oxygen concentrations in particular makes them essential to efficient large scale growth and expression of fermentation products. This video will briefly describe the advantages of the fermentor over the shake flask. It will also identify key components of a typical benchtop fermentation system and give basic instruction on setup of the vessel and calibration of its probes. The viewer will be familiarized with the sterilization process and shown how to inoculate the growth medium in the vessel with culture. Basic concepts of operation, sampling, and harvesting will also be demonstrated. Simple data analysis and system cleanup will also be discussed.     

Replating of bioreactor expanded human bone marrow results in extended growth of primitive and mature cells

The capability to expand human bone marrow mononuclear cells (BM MNC) in high density perfusion culture chambers (bioreactors) has recently been developed. In these bioreactors, total cell colony-forming unit-granulocyte/macrophage (CFU-GM), and long-term culture-initiating cell (LTC-IC) numbers increase significantly over a 14-day period. However, cell growth ceases after the 14-day period, possibly due to cell density limitations. Because of the remaining presence of early cells, it should be feasible to replate the cells and obtain continued expansion. In this study, we demonstrate that bioreactors generate cells, which upon replating into secondary bioreactors, lead to continued cell, CFU-GM, and LTC-IC₈ (measured after 8 weeks of secondary culture) expansion. A two-stage protocol, involving the replating of cells on days 9 to 12 of culture into new bioreators at the original seeding density, yielded greater than 50-fold cell expansion from BM MNC in 25 days. CFU-GM were expanded inhibitory factor (LIF) had no significant effect on total cells, CFU-GM, or LTC-IC₅ in this system. We conclude that two-stage bioreactor cultures are capable of supporting extended growth of human BM MNC, CFU-GM, and LTC-IC₈. The continued expansion of these primitive cells in the second stage of culture suggests that primitive cells with significant proliferative potential were generated in this system, and previous data on LTC-IC₅ expansion has now been extended to LTC-IC₈ expansion. Further optimization of culture conditions is likely to improve on the results obtained here, thus making perfusion bioreactor culture correspondingly more attractive for expanding BM MNC for BM transplantation.     

Cryopreservation of <Emphasis Type="Italic">Panax ginseng</Emphasis> Adventitious Roots

We tested desiccation and/or vitrification procedures to cryopreserve the adventitious roots of Panax ginseng, the source of commercially produced ginsenosides. When only desiccation was applied, the post-freeze survival of 3- to 4-mm root tips was <14% regardless of the composition of the preculture medium or the explant origin. Callus formation was frequently observed after cryopreservation. In contrast, 90% survival and 32.5% root formation efficiency were achieved after cryopreservation when a vitrification protocol was followed. Adventitious root cultures in flasks and bioreactors were reestablished from root tips cryopreserved by vitrification. A prolonged lag-phase and lower biomass production were recorded in post-freeze-regenerated cultures compared with control roots that were subcultured four times in flasks. However, biomass accumulations did not differ between control and regenerated roots at the end of the sixth subculturing period. After 40 days of culture in bioreactors, a mean value of 12.5 g dw L⁻¹ was recorded for post-freeze-regenerated cultures versus 9.1 g dw L⁻¹ for the control roots. Production of triol and diol ginsenosides in our bioreactor cultures also was enhanced after cryopreservation, by 41.0% and 89.8%, respectively. These results suggest that the vitrification method is successful for cryopreservation of P. ginseng adventitious roots.     

Dendritic cells derived from pluripotent stem cells:Potential of large scale production

Human pluripotent stem cells(hPSCs), including human embryonic stem cells and human induced pluripotent stem cells, are promising sources for hematopoietic cells due to their unlimited growth capacity and the pluripotency. Dendritic cells(DCs), the unique immune cells in the hematopoietic system, can be loaded with tumor specific antigen and used as vaccine for cancer immunotherapy. While autologous DCs from peripheral blood are limited in cell number, hPSC-derived DCs provide a novel alternative cell source which has the potential for large scale production. This review summarizes recent advances in differentiating hPSCs to DCs through the intermediate stage of hematopoietic stem cells. Step-wise growth factor induction has been used to derive DCs from hPSCs either in suspension cultureof embryoid bodies(EBs) or in co-culture with stromal cells. To fulfill the clinical potential of the DCs derived from hPSCs, the bioprocess needs to be scaled up to produce a large number of cells economically under tight quality control. This requires the development of novel bioreactor systems combining guided EB-based differentiation with engineered culture environment. Hence, recent progress in using bioreactors for hPSC lineage-specific differentiation is reviewed. In particular, the potential scale up strategies for the multistage DC differentiation and the effect of shear stress on hPSC differentiation in bioreactors are discussed in detail.     

动物细胞培养用生物反应器及相关技术

动物细胞大量培养是生产生物制品的重要途径,它用到的关键设备是生物反应器。根据培养细胞、培养载体、培养液混合方式的不同,生物反应器主要有搅拌式、气升式、中空纤维式、回转式等,其中搅拌式规模最大。回转式是NASA于20世纪90年代中期开发的一种新型生物反应器,被誉为空间生物反应器,可用于组织工程研究。与生物反应器配套的技术主要有灌注、微载体、多孔微球、转入抗凋亡基因等,可以有效地提高细胞密度,增加生物制品产量,提高质量。今后生物反应器研制主要朝两个方向发展:一是,以高密度培养动物细胞生产蛋白质药物为目的,二是以三维培养动物细胞(主要是人类细胞)再生组织或器官为目的。     

Immobilized Enzyme Three-Phase Reactors for Oxidation of Cephalosporin C

The enzymatic oxidation of Cephalosporin C (CEPHC) was catalyzed by D-aminoacid oxidase, from the red yeast Trigonopsis variabilis, immobilized on Duolite A365. The study was performed in two different three phase bioreactors, gas-liquid-solid (immobilized enzyme): the fluidized-bed batch reactor, fed continuously with oxygen and discontinuously with CEPHC, and the UF-membrane reactor continuously fed with both substrates. Only the first reactor allowed significant product yield (>70%) while the second was a very useful tool for laboratory investigation of both bioconversion kinetics and enzyme stability.

Optimum reaction temperature was 15d`C for the control of CEPHC spontaneous degradation (roughly 15% in 30 h), and enzyme deactivation (half-life greater than 30 h). Immobilization improved (one order of magnitude longer half-life) enzyme resistance to mechanical stresses induced by liquid stirring and gas bubbling. Roughly 0.04g of CEPHC was adsorbed per gram of enzyme carrier. The limiting step in oxygen transfer was the gas to liquid transport. In order to attain kinetic control of the bioconversion the mildest conditions were atmospheric gas pressure and oxygen flow rate equal to 2 × 10 ²NmL/s per mL of liquid phase.     

Modular bioreactor for primary human hepatocyte culture: medium flow stimulates expression and activity of detoxification genes

Down-regulation of detoxification genes, notably cytochrome P450 (CYPs), in primary hepatocyte cultures is a long-standing and major concern. We evaluated the influence of medium flow in this model. Hepatocytes isolated from 12 different liver donors were cultured either in a multichamber modular bioreactor (MCmB, flow rate 250-500 μL/min) or under standard/static conditions, and the expression of 32 genes, enzyme activities and biological parameters were measured 7-21 days later. mRNA expression of genes involved in xenobiotic/drug metabolism and transport, including CYP1A1, 1A2, 2B6, 2C9, 3A4 (and activities for some of them), UDP-glucuronosyltransferase (UGT) 1A1, UGT2B4, UGT2B7, glutathione S-transferase (GSTα), and multidrug resistance protein 1 (MDR1) and MRP2, were specifically up-regulated by medium flow as compared with static controls in all cultures tested. In 2-week-old cultures, expression of detoxification genes reached levels close to or higher than those measured in freshly isolated hepatocytes. In contrast, CYP2D6 and most of other tested genes were not affected by medium flow. We conclude that medium flow specifically interferes with, and up-regulates, the activity of xenosensors and/or the expression of detoxification genes in primary human hepatocytes. Down-regulation of detoxification genes in conventional (static) cultures is therefore partly a consequence of the absence of medium circulation.     

植物细胞生物反应器培养的研究进展(I)

利用植物细胞大规模悬浮培养生产植物有用代谢产物在近些年来取得了很大发展,但植物细胞悬浮培养的工业化应用受到来自生物及工程技术上的限制.本文针对植物细胞培养的基本特点,详细讨论了与大规模生产有关的工程技术方面的问题,如植物细胞聚集、溶氧及气体成分、流体性能、剪切力对植物细胞培养产生的影响.     

Effect of pH on the stability of Pleurotus eryngii versatile peroxidase during heterologous production in Emericella nidulans

Complementary DNA (cDNA) encoding the new versatile peroxidase from the ligninolytic basidiomycete Pleurotus eryngii has been expressed in the ascomycete Emericella nidulans. In recombinant E. nidulans cultures, the pH reached values as high as 8.3, correlating with a sharp decrease in peroxidase activity. Peroxidase was rapidly inactivated at alkaline pH, but was comparatively stable at acidic pH. The peroxidase inactivation in alkaline buffer could be reversed by adding Ca²⁺ and lowering the pH. However, reactivation did not result after incubating the enzyme in non-buffered E. nidulans cultures that reached pH 7.5. To optimize recombinant peroxidase production, the effect of controlling the pH in E. nidulans bioreactor cultures was studied. An extended growth period, and a significant increase in the recombinant peroxidase level (5.3-fold higher activity than in the bioreactor without pH control) was obtained when the pH was maintained at 6.8, showing that culture pH is an important parameter for recombinant peroxidase production.     

A bioreactor model system specifically designed for <Emphasis Type="Italic">Tetrahymena</Emphasis> growth and cholesterol removal from milk

This work describes the configuration and operation of a bioreactor system especially designed for Tetrahymena cultivation and its use for milk improvement, particularly cholesterol elimination by the action of this cell. An advantage of the proposed method is the re-use of the growth medium; thus, the medium is used twice to provide two batches of Tetrahymena biomass without the need of further inoculation. This makes the procedure of producing the cell biomass faster and more economical. Cells are concentrated in the culture vessels by sedimentation at room temperature and then transferred to milk suspensions, where they can further grow for at least one generation with the benefit of reducing steeply cholesterol level. Milk treated according to this process is separated from the biomass by centrifugation. Under these conditions, less than 5% of the cells remain in the milk, and cholesterol elimination amounts to 75 +/- 10% of that initially present. No changes in sensorial properties of the milk, such as clotting or butyric odor, were observed as a result of this treatment. In addition, the bioreactor allows the aseptic recovery of the spent growth medium, which contains diverse enzymes of interest, and the cell pellets, to exploit particular lipids like phosphonolipids, abundant poly-unsaturated fatty acids and co-enzyme Q(8).