Production of a secreted glycoprotein from an inducible promoter system in a perfusion bioreactor

The primary advantage of an inducible promoter expression system is that production of the recombinant protein can be biochemically controlled, allowing for the separation of unique growth and production phases of the culture. During the growth phase, the culture is rapidly grown to high cell density prior to induction without the extra metabolic burden of exogenous protein production, thus minimizing the nonproductive period of the culture. Induction of the culture at high cell density ensures that the volumetric production will be maximized. In this work, we have demonstrated the feasibility of overexpressing a reporter glycoprotein from the inducible MMTV promoter in recombinant Chinese hamster ovary (CHO) cells cultured in a high cell density perfusion bioreactor system. Retention of suspension-adapted CHO cells was achieved by inclined sedimentation. To maximize volumetric production of the culture, we have demonstrated that high cell density must be achieved prior to induction. This operating scheme resulted in a 10-fold increase in volumetric titer over the low density induction culture, corresponding directly to a 10-fold increase in viable cell density during the highly productive period of the culture. The amount of glycoprotein produced in this high cell density induction culture during 26 days was 84-fold greater than that produced in a week long batch bioreactor. Long-term perfusion cultures of the recombinant cell line showed a production instability, a phenomenon that is currently being investigated.     

Effect of surfactant pluronic F-68 on CHO cell growth, metabolism, production, and glycosylation of human recombinant IFN-γ in mild operating conditions

The control of glycosylation to satisfy regulatory requirements and quality consistency of recombinant proteins produced by different processes has become an important issue. With two N-glycosylation sites, γ-interferon (IFN-γ) can be seen as a prototype of a recombinant therapeutic glycoprotein for this purpose. The effect of the nonionic surfactant Pluronic F-68 (PF-68) on cell growth and death was investigated, as well as production and glycosylation of recombinant IFN-γ produced by a CHO cell line that was maintained in a rich protein-free medium in the absence or presence of low agitation. Under these conditions, a dose-dependent effect of PF-68 (0-0.1%) was shown not only to significantly enhance growth but also to reduce cell lysis. Interestingly, supplementing the culture medium with PF-68 led to increased IFN-γ production as a result of both higher cell densities and a higher specific production rate of IFN-γ. If cells were grown with agitation, lack of PF-68 in the culture medium decreased the fraction of the fully glycosylated IFN-γ glycoform (2N) from 80% to 65-70% during the initial period. This effect appeared to be due to a lag phase in cell growth observed during this period. Finally, a global kinetic study of CHO cell metabolism indicated higher efficiency in the utilization of the two major carbon substrates when cultures were supplemented with PF-68. Therefore, these results highlight the importance of understanding how media surfactant can affect cell growth as well as cell death and the product quality of a recombinant glycoprotein expressed in CHO cell cultures.     

Stainless steel mesh supports high density cell growth and production of recombinant Mullerian Inhibiting Substances

Summary Stainless steel mesh supported the high density growth of anchorage dependent CHO fibroblasts without the use of a special culture system. CHO cells, designated B-9, containing an amplified genomic construct of the human gene for Mullerian Inhibiting Substance (MIS), grew to a high confluent density on stainless steel meshwork while producing substantial amounts of human recombinant MIS over a long period of time. The mesh could be easily coated with various extracellular matrix proteins, such as Laminin, Fibronectin, Collagen or Matrigel, which permitted the testing of the effects of surface modifications on cell yield and recombinant protein production. Since the amount of medium per surface area required for optimal cell growth is lower than for some large volume cell culture methods, media costs can be reduced using mesh. In addition, no special cell culture equipment or complex manipulations are required. Thus, the use of meshwork for anchorage-dependent cells can increase the efficiency of growth and decrease the cost of recombinant protein production. This work is supported by NIH grant CA 17393 and American Cancer Society grant PDT 221A to P. K. D. and NIH grant EY 06535 to J. E. Editor's Statement This approach to large scale, high density cultivation of cells, one of several which are based on increasing surface area of the cultures, allows the production of large amounts of recombinant product within a research laboratory with modest bulk culture capability.     

A quantitative proteomic analysis of cellular responses to high glucose media in Chinese hamster ovary cells

A goal in recombinant protein production using Chinese hamster ovary (CHO) cells is to achieve both high specific productivity and high cell density. Addition of glucose to the culture media is necessary to maintain both cell growth and viability. We varied the glucose concentration in the media from 5 to 16 g/L and found that although specific productivity of CHO‐DG44 cells increased with the glucose level, the integrated viable cell density decreased. To examine the biological basis of these results, we conducted a discovery proteomic study of CHO‐DG44 cells grown under batch conditions in normal (5 g/L) or high (15 g/L) glucose over 3, 6, and 9 days. Approximately 5,000 proteins were confidently identified against an mRNA‐based CHO‐DG44 specific proteome database, with 2,800 proteins quantified with at least two peptides. A self‐organizing map algorithm was used to deconvolute temporal expression profiles of quantitated proteins. Functional analysis of altered proteins suggested that differences in growth between the two glucose levels resulted from changes in crosstalk between glucose metabolism, recombinant protein expression, and cell death, providing an overall picture of the responses to high glucose environment. The high glucose environment may enhance recombinant dihydrofolate reductase in CHO cells by up‐regulating NCK1 and down‐regulating PRKRA, and may lower integrated viable cell density by activating mitochondrial‐ and endoplasmic reticulum‐mediated cell death pathways by up‐regulating HtrA2 and calpains. These proteins are suggested as potential targets for bioengineering to enhance recombinant protein production. © 2015 American Institute of Chemical Engineers Biotechnol. Prog., 31:1026–1038, 2015     

Serum- and protein-free media formulations for the Chinese hamster ovary cell line DUKXB11

The production of therapeutic proteins in mammalian cell lines is of outstanding importance. The maintenance of most mammalian cell lines in culture requires the addition of serum to the culture medium. The elimination of serum from mammalian cell culture is desirable since serum is expensive and a source of contaminants, e.g. viruses, mycoplasma or prions. Here we describe the composition of serum- and protein-free media for the Chinese hamster ovary (CHO) cell line DUKXB11. The serum-free formulation supports excellent growth of CHO DUKXB11 cells at low (23cells/cm2) and high (2 x 10(4) cells/cm2) seeding densities characterized by a generation time of 10-12h, and, after addition of 0.2% pluronic F-68, the growth of a recombinant suspension cell line derived from DUKXB11. In addition, this formulation also allowed us to adapt recombinant cell lines expressing various amounts of human antithrombin ATIII (ATIII) to serum-free conditions. Secretion of ATIII was readily observed in the serum-free medium. Minor changes to the serum-free formulation resulted in a protein free formulation that supported growth of CHO DUKXB11 cells, growth of recombinant CHO cells expressing ATIII, and production of ATIII.     

微囊化重组CHO细胞制备和培养条件的优化

微囊化重组基因细胞移植治疗肿瘤是一种新兴的肿瘤基因治疗方法,然而由于目前微囊化细胞规模化制备和培养技术还不成熟,阻碍了其在临床治疗中的推广与应用。以重组CHO细胞为模型,考察了不同的微囊制备和培养条件对微囊化细胞生长和内皮抑素表达的影响。实验表明,种子细胞所处的生长阶段和细胞接种密度对微囊化细胞生长和内皮抑素表达的影响较大,对数生长期的细胞进行包囊并且细胞接种密度为1×106~2×106cells/mL微囊时微囊内细胞生长良好、内皮抑素表达量高。微囊制备时间对细胞活性和内皮抑素表达也有较大的影响,制备时间延长对细胞的损伤增大,因此制备时间应控制在5h以内。生物微胶囊在制备过程中会造成细胞损伤,而体外培养是恢复细胞活性的良好方法,在培养过程中微囊接种量为5%时对细胞生长和内皮抑素表达有利。     

重组蛋白在中国仓鼠卵巢细胞中高效表达的影响因素

高效表达重组蛋白 ,对于生物制药意义重大。大多数药用蛋白是糖蛋白 ,中国仓鼠卵巢细胞 (Chinesehamsterovarycell,CHO)是目前重组糖基蛋白生产的首选体系。影响外源蛋白在CHO细胞中表达的因素很多 ,从CHO细胞表达体系、表达载体系统、外源基因、表达细胞株的加压扩增与筛选、细胞大规模培养等方面对CHO高效表达加以阐述 ,同时提出存在的问题和未来的发展方向。     

Improving the efficiency of CHO cell line generation using glutamine synthetase gene knockout cells

Although Chinese hamster ovary (CHO) cells, with their unique characteristics, have become a major workhorse for the manufacture of therapeutic recombinant proteins, one of the major challenges in CHO cell line generation (CLG) is how to efficiently identify those rare, high‐producing clones among a large population of low‐ and non‐productive clones. It is not unusual that several hundred individual clones need to be screened for the identification of a commercial clonal cell line with acceptable productivity and growth profile making the cell line appropriate for commercial application. This inefficiency makes the process of CLG both time consuming and laborious. Currently, there are two main CHO expression systems, dihydrofolate reductase (DHFR)‐based methotrexate (MTX) selection and glutamine synthetase (GS)‐based methionine sulfoximine (MSX) selection, that have been in wide industrial use. Since selection of recombinant cell lines in the GS‐CHO system is based on the balance between the expression of the GS gene introduced by the expression plasmid and the addition of the GS inhibitor, L‐MSX, the expression of GS from the endogenous GS gene in parental CHOK1SV cells will likely interfere with the selection process. To study endogenous GS expression's potential impact on selection efficiency, GS‐knockout CHOK1SV cell lines were generated using the zinc finger nuclease (ZFN) technology designed to specifically target the endogenous CHO GS gene. The high efficiency (～2%) of bi‐allelic modification on the CHO GS gene supports the unique advantages of the ZFN technology, especially in CHO cells. GS enzyme function disruption was confirmed by the observation of glutamine‐dependent growth of all GS‐knockout cell lines. Full evaluation of the GS‐knockout cell lines in a standard industrial cell culture process was performed. Bulk culture productivity improved two‐ to three‐fold through the use of GS‐knockout cells as parent cells. The selection stringency was significantly increased, as indicated by the large reduction of non‐producing and low‐producing cells after 25 µM L‐MSX selection, and resulted in a six‐fold efficiency improvement in identifying similar numbers of high‐productive cell lines for a given recombinant monoclonal antibody. The potential impact of GS‐knockout cells on recombinant protein quality is also discussed. Biotechnol. Bioeng. 2012; 109:1007–1015. © 2011 Wiley Periodicals, Inc.     

Engineering Chinese hamster ovary (CHO) cells to achieve an inverse growth – associated production of a foreign protein, β-galactosidase

Protein synthesis in mammalian cells can be observed in two strikingly different patterns: 1) production of monoclonal antibodies in hybridoma cultures is typically inverse growth associated and 2) production of most therapeutic glycoproteins in recombinant mammalian cell cultures is found to be growth associated. Production of monoclonal antibodies has been easily maximized by culturing hybridoma cells at very low growth rates in high cell density fed- batch or perfusion bioreactors. Applying the same bioreactor techniques to recombinant mammalian cell cultures results in drastically reduced production rates due to their growth associated production kinetics. Optimization of such growth associated production requires high cell growth conditions, such as in repeated batch cultures or chemostat cultures with attendant excess biomass synthesis. Our recent research has demonstrated that this growth associated production in recombinant Chinese hamster ovary (CHO) cells is related to the S (DNA synthesis)-phase specific production due to the SV40 early promoter commonly used for driving the foreign gene expression. Using the stably transfected CHO cell lines synthesizing an intracellular reporter protein under the control of SV40 early promoter, we have recently demonstrated in batch and continuous cultures that the product synthesis is growth associated. We have now replaced this S-phase specific promoter in new expression vectors with the adenovirus major late promoter which was found to be active primarily in the G1-phase and is expected to yield the desirable inverse growth associated production behavior. Our results in repeated batch cultures show that the protein synthesis kinetics in this resulting CHO cell line is indeed inverse growth associated. Results from continuous and high cell density perfusion culture experiments also indicate a strong inverse growth associated protein synthesis. The bioreactor optimization with this desirable inverse growth associated production behavior would be much simpler than bioreactor operation for cells with growth associated production. This revised version was published online in August 2006 with corrections to the Cover Date.     

Microarray platform affords improved product analysis in mammalian cell growth studies

High throughput (HT) platforms serve as a cost‐efficient and rapid screening method for evaluating the effect of cell‐culture conditions and screening of chemicals. We report the development of a HT cell‐based microarray platform to assess the effect of culture conditions on Chinese hamster ovary (CHO) cells. Specifically, growth, transgene expression and metabolism of a GS/methionine sulphoximine (MSX) CHO cell line, which produces a therapeutic monoclonal antibody, was examined using a microarray system in conjunction with a conventional shake flask platform in a non‐proprietary medium. The microarray system consists of 60‐nL spots of cells encapsulated in alginate and separated in groups via an 8‐well chamber system attached to the chip. Results show the non‐proprietary medium developed allows cell growth, production, and normal glycosylation of recombinant antibody and metabolism of the recombinant CHO cells in both the microarray and shake flask platforms. In addition, 10.3 mM glutamate addition to the defined base medium results in lactate metabolism shift in the recombinant GS/MSX CHO cells in the shake flask platform. Ultimately, the results demonstrate that the HT microarray platform has the potential to be utilized for evaluating the impact of media additives on cellular processes, such as cell growth, metabolism, and productivity.     

表达内皮抑素的rCHO细胞的微囊化培养

微囊化重组基因细胞移植治疗肿瘤是一种新兴的肿瘤基因治疗方法,如果将此技术应用到临床研究,就需要制备大量的细胞活性良好、重组蛋白表达量高的生物微胶囊。种子细胞是生物微胶囊治疗作用的执行者, 是构建微囊微反应器的基本元素。如何获得大量高活性的种子细胞已经成为规模化制备生物微胶囊所面临的最关键的限制因素。本实验考察了搅拌式生物反应器内扩增的重组CHO细胞进行包囊及微囊化细胞在生物反应器内规模化培养的可行性。实验结果显示:重组CHO细胞在生物反应器内可以快速生长,并且对数期细胞包囊,微囊化细胞活性良好。制备的微囊化细胞可以在生物反应器内培养,与培养板培养比较细胞生长较快、内皮抑素表达量较高。应用生物反应器培养技术能够在体外快速、大量扩增重组CHO细胞,满足微囊化细胞制备对种子细胞量与质的要求,微囊化细胞可以在生物反应器内培养。     

Temperature control of growth and productivity in mutant Chinese hamster ovary cells synthesizing a recombinant protein

The use of a temperature switch to control the growth and productivity of temperature-sensitive (ts) mutants was investigated to extend the productive life span of recombinant Chinese hamster ovary (CHO) cells in batch culture. Bromodeoxyuridine was used at 39 degrees C to select mutagenized CHO-K1 cells, which resulted in the isolation of 31 temperature-sensitive mutants that were growth inhibited at 39 degrees C. Two of these mutants were successfully transfected with the gene for tissue inhibitor of metalloproteinases (TIMP) using glutamine synthetase amplification, and a permanent recombinant cell line established (5G1-B1) that maintains the ts phenotype.Continuous exposure to the nonpermissive temperature (npt) of 39 degrees C led to a rapid decline in cell viability. However, a temperature regime using alternating incubations at 34 degrees C and 39 degrees C arrested the 5G1-B1 cells while retaining a high cell viability for up to 170 h in culture. The specific production rate of the growth-arrested cells was 3-4 times that of control cultures maintained at a constant 34 degrees C over the crucial 72-130-h period of culture, which resulted in a 35% increase in the maximum product yield. Glucose uptake and lactate production both decreased in arrested cells. Flow cytometric analysis indicated that 5G1-B1 cells arrested in the G(1) or G(0) phase of the cell cycle, and no major structural damage was caused to these cells by the alternating temperature regime.These results demonstrate that growth-arrested ts CHO cells have increased productivity compared to growing cultures and maintain viability for longer periods. The system offers the prospect of enhancing the productivity of recombinant mammalian cells grown in simple batch fermentors. (c) 1993 John Wiley & Sons, Inc.     

Determination of Chinese hamster ovary cell line stability and recombinant antibody expression during long-term culture

Chinese hamster ovary (CHO) cell lines are frequently used as hosts for the production of recombinant therapeutics, such as monoclonal antibodies, due to their ability to perform correct post-translational modifications. A potential issue when utilizing CHO cells for therapeutic protein production is the selection of cell lines that do not retain stable protein expression during long-term culture (LTC). Instability of expression impairs process yields, effective usage of time and money, and regulatory approval for the desired therapeutic. In this study, we investigated a model unstable GS-CHO cell line over a continuous period of approximately 100 generations to determine markers of mechanisms that underlie instability. In this cell line, stability of expression was retained for 40-50 generations after which time a 40% loss in antibody production was detected. The instability observed within the cell line was not due to a loss in recombinant gene copy number or decreased expression of mRNA encoding for recombinant antibody H or L chain, but was associated with lower cumulative cell time values and an apparent increased sensitivity to cellular stress (exemplified by increased mRNA expression of the stress-inducible gene GADD153). Changes were also noted in cellular metabolism during LTC (alterations to extracellular alanine accumulation, and enhanced rates of glucose and lactate utilization, during the exponential and decline phase of batch culture, respectively). Our data indicates the breadth of changes that may occur to recombinant CHO cells during LTC ranging from instability of recombinant target production at a post-mRNA level to metabolic events. Definition of the mechanisms, regulatory events, and linkages underpinning cellular phenotype changes require further detailed analysis at a molecular level.     

A comprehensive comparison of mixing, mass transfer, Chinese hamster ovary cell growth, and antibody production using Rushton turbine and marine impellers

Large scale production of monoclonal antibodies has been accomplished using bioreactors with different length to diameter ratios, and diverse impeller and sparger designs. The differences in these physical attributes often result in dissimilar mass transfer, mechanical stresses due to turbulence and mixing inside the bioreactor that may lead to disparities in cell growth and antibody production. A rational analysis of impeller design parameters on cell growth, protein expression levels and subsequent antibody production is needed to understand such differences. The purpose of this study was to examine the impact of Rushton turbine and marine impeller designs on Chinese hamster ovary (CHO) cell growth and metabolism, and antibody production and quality. Experiments to evaluate mass transfer and mixing characteristics were conducted to determine if the nutrient requirements of the culture would be met. The analysis of mixing times indicated significant differences between marine and Rushton turbine impellers at the same power input per unit volume of liquid (P/V). However, no significant differences were observed between the two impellers at constant P/V with respect to oxygen and carbon dioxide mass transfer properties. Experiments were conducted with CHO cells to determine the impact of different flow patterns arising from the use of different impellers on cell growth, metabolism and antibody production. The analysis of cell culture data did not indicate any significant differences in any of the measured or calculated variables between marine and Rushton turbine impellers. More importantly, this study was able to demonstrate that the quality of the antibody was not altered with a change in the impeller geometry.     

Effect of culture temperature on a recombinant CHO cell line producing a C-terminal α-amidating enzyme

In order to seek an efficient method for producing a recombinant protein by using animal cell culture, we investigated various effects of the culture temperature on a recombinant CHO cell line (3μ-1S), producing a C-terminal α-amidating enzyme (799BglIIα-AE) originating from Xenopus laevis. The results revealed that a low culture temperature (below 37 °C) led to the following phenomena: [1] inhibited cell growth, [2] enhanced cellular productivity of the recombinant protein, [3] maintained high cell viability, [4] suppressed medium consumption, and [5] suppressed release of impurities from the cells. These findings indicate that a quite simple method, the culture at low temperature, will contribute to the total improvement of the industrial process for the production of the recombinant protein, 799BglIIα-AE. This revised version was published online in August 2006 with corrections to the Cover Date.     

Mitochondrial aconitase is a key regulator of energy production for growth and protein expression in Chinese hamster ovary cells

Introduction

Mammalian cells like Chinese hamster ovary (CHO) cells are routinely used for production of recombinant therapeutic proteins. Cells require a continuous supply of energy and nutrients to sustain high cell densities whilst expressing high titres of recombinant proteins. Cultured mammalian cells are primarily dependent on glucose and glutamine metabolism for energy production.

Objectives

The TCA cycle is the main source of energy production and its continuous flow is essential for cell survival. Modulated regulation of TCA cycle can affect ATP production and influence CHO cell productivity.

Methods

To determine the key metabolic reactions of the cycle associated with cell growth in CHO cells, we transiently silenced each gene of the TCA cycle using RNAi.

Results

Silencing of at least four TCA cycle genes was detrimental to CHO cell growth. With an exception of mitochondrial aconitase (or Aco2), all other genes were associated with ATP production reactions of the TCA cycle and their resulting substrates can be supplied by other anaplerotic and cataplerotic reactions. This study is the first of its kind to have established key role of aconitase gene in CHO cells. We further investigated the temporal effects of aconitase silencing on energy production, CHO cell metabolism, oxidative stress and recombinant protein production.

Conclusion

Transient silencing of mitochondrial aconitase inhibited cell growth, reduced ATP production, increased production of reactive oxygen species and reduced cell specific productivity of a recombinant CHO cell line by at least twofold.

     

Isolation, characterization and recombinant protein expression in Veggie-CHO: A serum-free CHO host cell line

The dihydrofolate reductase-deficient Chinese hamster ovary cell line, DXB11-CHO, commonly used as a host cell for the production of recombinant proteins requires 7.5% serum-supplementation for optimal growth. Regulatory issues surrounding the use of serum in clinical production processes and the direct and indirect costs of using serum in large-scale production and recovery processes have triggered efforts to derive serum-independent host cell lines. We have successfully isolated a serum-free host that we named Veggie- CHO. Veggie-CHO was generated by adapting DXB11-CHO cells to growth in serum-free media in the absence of exogenous growth factors such as Transferrin and Insulin-like growth factor, which we have previously shown to be essential for growth and viability of DXB11- CHO cells. Veggie-CHO cells have been shown to maintain an average doubling time of 22 hr in continuous growth cultures over a period of three months and have retained the dihydrofolate reductase -deficient phenotype of their parental DXB11-CHO cells. These properties and the stability of its serum-free phenotype have allowed the use of Veggie- CHO as host cells for transfection and amplified expression of recombinant proteins. We describe the derivation a serum-free recombinant cell line with an average doubling time of 20 hr and specific productivity of 2.5 Units recombinant Flt-3L protein per 10e6 cells per day. This revised version was published online in August 2006 with corrections to the Cover Date.