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  • Articles  (29)
  • cell culture
  • 1995-1999  (29)
  • Process Engineering, Biotechnology, Nutrition Technology  (29)
  • Electrical Engineering, Measurement and Control Technology
  • 1
    Electronic Resource
    Electronic Resource
    Springer
    Cytotechnology 19 (1995), S. 95-105 
    ISSN: 1573-0778
    Keywords: antibiotics ; cell culture
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract This article describes the historical development of the prophylactic use of antibiotics in cell culture as well as their effects on cells. The influence of antibiotics on cell morphology, cellular degeneration and cell death and cellular function is summarized. Cellular DNA as well as protein synthesis are affected which can lead to interference with, or even changes in, metabolic processes. Such effects must be considered in cell culture research. As antibiotics are used in multifold ways, the otherwise standardized conditions in cell culture are no longer comparable. The prophylactic use of antibiotics is rejected for scientific reasons.
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  • 2
    ISSN: 1573-0778
    Keywords: cell culture ; half-life ; packaging cells ; retrovirus ; titer ; ΨCRIP
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Rapidly expanding development and practice of gene therapy requires the availability of large quantities of high titer retroviral supernatants. One way to achieve high retroviral titers is through improved understanding of the kinetics of retroviral production and decay, and the subsequent development of improved cell culture methods. In the present study we investigated the effects of different operational modes on the retroviral production of the NIH 3T3 fibroblast derived amphotropic murine retroviral producing cell line pMFG/ΨCRIP. Semi-continuous culture (exchange of 50% of medium volume daily) was found to promote cell growth and enhance retroviral production. The rapid medium exchange resulted in significantly larger amounts of high titer supernatants and an extended production phase as compared to the batch control cultures. The specific viral productivity of the pMFG/ΨCRIP cells was in the range of 10 to 40 infectious viruses produced per thousand producer cells per day. The CV-1 African Green Monkey kidney cell line was used as the infection target. Lowering the serum level form 20% to 10% improved retroviral production slightly. However, at lower serum levels (1%, 5% and 10% (v/v)) growth of the producer cell line, and thus retroviral production, was directly proportional to the serum level. The half-life of the virus at 37°C was found to be 5.5 hours. Promoting the growth of producer cell lines can improve retroviral vectors titers and viral production. High cell density systems that allow for rapid cell growth and waste product removal are likely to be used to generate high-titer retroviral supernatants.
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  • 3
    ISSN: 1573-0778
    Keywords: cell culture ; mixing time ; oxygen demand ; oxygen transfer ; pH and dO2 sensitivity ; scale-up
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Because of concern for cell damage, very low agitation energy inputs have been used in industrial animal cell bioreactors, typical values being two orders of magnitude less than those found in bacterial fermentations. Aeration rates are also very small. As a result, such bioreactors might be both poorly mixed and also unable to provide the higher oxygen up-take rates demanded by more intensive operation. This paper reports experimental studies both of K L a and of mixing (via pH measurements) in bioreactors up to 8 m3 at Wellcome and of scaled down models of such reactors at Birmingham. Alongside these physical measurements, sensitivity of certain cell lines to continuously controlled dO2 has been studied and the oxygen up-take rates measured in representative growth conditions. An analysis of characteristic times and mixing theory, together with other recent work showing that more vigorous agitation and aeration can be used especially in the presence of Pluronic F-68, indicates ways of improving their performance. pH gradients offer a special challenge.
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  • 4
    Electronic Resource
    Electronic Resource
    Springer
    Cytotechnology 22 (1996), S. 3-16 
    ISSN: 1573-0778
    Keywords: cell culture ; process monitoring ; oxygenation ; CO2 transfer ; aggregation ; segregation ; diffusion, on-line monitoring
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract High density cell culture systems offer the advantage of production of bio-pharmaceuticals in compact bioreactors with high volumetric production rates; however, these systems are difficult to design and operate. First of all, the cells have to be retained in the bioreactor by physical means during perfusion. The design of the cell retention is the key to performance of high density cell culture systems. Oxygenation and media design are also important for maximizing the cell number. In high density perfusion reactors, variable cell density, and hence the metabolic demand, require constant adjustment of perfusion rates. The use of cell specific perfusion rate (CSPR) control provides a constant environment to the cells resulting in consistent production. On-line measurement of cell density and metabolic activities can be used for the estimation of cell densities and the control of CSPR. Issues related to mass transfer and mixing become more important at high cell densities. Due to the difference in mass transfer coefficients for oxygen and CO2, a significant accumulation of dissolved CO2 is experienced with silicone tubing aeration. Also, mixing is observed to decrease at high densities. Base addition, if not properly done, could result in localized cell lysis and poor culture performance. Non-uniform mixing in reactors promotes the heterogeneity of the culture. Cell aggregation results in segregation of the cells within different mixing zones. This paper discusses these issues and makes recommendations for further development of high density cell culture bioreactors.
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  • 5
    Electronic Resource
    Electronic Resource
    Springer
    Cytotechnology 31 (1999), S. 3-8 
    ISSN: 1573-0778
    Keywords: cell culture ; livestock ; milk ; nuclear transfer ; transgenic
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Transgenesis may allow the generation of farm animals with altered phenotype, animal models for research and animal bioreactors. Although such animals have been produced, the time and expense involved in generating transgenic livestock and then evaluating the transgene expression pattern is very restrictive. If questions about the ability and efficiency of expression could be asked solely in vitro rapid progress could be achieved. Unfortunately, experiments addressing transcriptional control in vitro have proved unreliable in their ability to indicate whether a transgene will be transcribed or not. However, initial studies suggest that cell culture may be able to predict in vivo post-transcriptional events. We review these issues and propose that strategies which engineer the transgene integration site could enhance the probability for efficient expression. This approach has now become feasible with the development of techniques allowing animals to be generated from somatic cells by nuclear transfer. The important step in this procedure is the use of cells grown in culture as the source of genetic information, allowing the selection of specific transgene integration events. This technology which has dramatically increased the potential use of transgenic livestock for both agricultural and biotechnological applications, is based on standard cell culture methodology. We are now at the start of a new era in large animal transgenics.
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  • 6
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 51 (1996), S. 399-409 
    ISSN: 0006-3592
    Keywords: cell damage ; cell culture ; bubble aeration ; agitation ; bubble coalescence and breakup ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: It has been established that the forces resulting from bubbles rupturing at the free air (gas)/liquid surface injure animal cells in agitated and/or sparged bioreactors. Although it has been suggested that bubble coalescence and breakup within agitated and sparged bioreactors (i.e., away from the free liquid surface) can be a source of cell injury as well, the evidence has been indirect. We have carried out experiments to examine this issue. The free air/liquid surface in a sparged and agitated bioractor was eliminated by completely filling the 2-L reactor and allowing sparged bubbles to escape through an outlet tube. Two identical bioreactors were run in parallel to make comparisons between cultures that were oxygenated via direct air sparging and the control culture in which silicone tubing was used for bubble-free oxygenation. Thus, cell damage from cell-to-bubble interactions due to processes (bubble coalescence and breakup) occurring in the bulk liquid could be isolated by eliminating damage due to bubbles rupturing at the free air/liquid surface of the bioreactor. We found that Chinese hamster ovary (CHO) cells grown in medium that does not contain shear-protecting additives can be agitated at rates up to 600 rpm without being damaged extensively by cell-to bubble interactions in the bulk of the bioreactor. We verified this using both batch and high-density perfusion cultures. We tested two impeller designs (pitched blade and Rushton) and found them not to affect cell damage under similar operational conditions. Sparger location (above vs. below the impeller) had no effect on cell damage at higher agitation rates but may affect the injury process at lower agitation intensities (here, below 250 rpm). In the absence of a headspace, we found less cell damage at higher agitation intensities (400 and 600 rpm), and we suggest that this nonintuitive finding derives from the important effect of bubble size and foam stability on the cell damage process. © 1996 John Wiley & Sons, Inc.
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  • 7
    ISSN: 1573-0778
    Keywords: apoptosis ; bcl-2 ; cell culture ; chloramphenicol acetyltransferase ; recombinant protein ; Sindbis virus
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Viruses carrying foreign genes are often used for the production of recombinant proteins in mammalian cells and other eukaryotic expression systems. Though high levels of gene expression are possible using viral vectors, the host cell generally responds to the infection by inducing apoptotic cell death within several days, abruptly ending protein production. It has recently been demonstrated, however, that apoptosis can be suppressed in virally infected cells using anti-apoptotic genes, such as bcl-2. In this study, stably transfected rat carcinomal cell lines, AT3-bcl2 and AT3-neo, were infected with a Sindbis virus carrying the gene for chloramphenicol acetyltransferase (CAT) in an effort to determine the effect of bcl-2 on cell viability and recombinant protein production. Infected AT3-bcl2 cells consistently maintained viabilities close to 100% and a growth rate equivalent to that of uninfected cells (0.040 h-1). In contrast, the Sindbis viral vector induced apoptosis in the AT3-neo cells, which were all dead by three days post-infection. Though infected AT3-neo cells generated higher levels of heterologous protein, over 1000 mUnits per well, CAT activity fell to zero by two days post-infection. In contrast, chloramphenicol acetyltransferase was present in AT3-bcl2 cells for almost a week, reaching a maximum level of 580 mUnits per well. In addition, recombinant protein production in AT3-bcl2 cells was extended and amplified by the regular addition of virus to the culture medium, a process which resulted in expression for the duration of the cell culture process.
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  • 8
    Electronic Resource
    Electronic Resource
    Springer
    Cytotechnology 22 (1996), S. 263-267 
    ISSN: 1573-0778
    Keywords: biodegradable ; bone regeneration ; cell culture ; human cell osteoblasts ; polymers
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract The care of patients with a skeletal deficiency currently involves the use of bone graft or a non-biologic material such as a metal or polymer. There are alternate possibilities in development which involve the growth of bone cells (osteoblasts) on degradable polymer scaffolds. These tissue engineering strategies require production of the polymeric scaffold, cellular harvest followed by either ex vivo or in vivo growth of the cells on the scaffold, and exploration of the interaction between the cell and scaffold. Research into these strategies utilizes cells from a variety of species, but clinical applications will likely require human osteoblasts. This study explores the process whereby human osteoblasts are harvested under sterile conditions during joint replacement surgery from normally discarded cancellous bone, transported from the operating room to the lab, and grown in culture. This process is feasible, and the cells express their phenotype via the production of alkaline phosphatase and collagen in culture.
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  • 9
    ISSN: 1573-0778
    Keywords: CHO ; IGF-I ; serum-free ; autocrine growth ; cell culture
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Insulin-like growth factor I has similar mitogenic effects to insulin, a growth factor required by most cells in culture, and it can replace insulin in serum-free formulations for some cells. Chinese Hamster Ovary cells grow well in serum-free medium with insulin and transferrin as the only exogenous growth factors. An alternative approach to addition of exogenous growth factors to serum-free medium is transfection of host cells with growth factor-encoding genes, permitting autocrine growth. Taking this approach, we constructed an IGF-I heterologous gene driven by the cytomegalovirus promoter, introduced it into Chinese Hamster Ovary cells and examined the growth characteristics of Insulin-like growth factor I-expressing clonal cells in the absence of the exogenous factor. The transfected cells secreted up to 500 ng/106 cells/day of mature Insulin-like growth factor I into the conditioned medium and as a result they grew autonomously in serum-free medium containing transferrin as the only added growth factor. This growth-stimulating effect, observed under both small and large scale culture conditions, was maximal since no further improvement was observed in the presence of exogenous insulin.
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  • 10
    ISSN: 1573-0778
    Keywords: cell culture ; polymerase chain reaction ; retrovirus ; reverse transcriptase
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Reverse transcriptase (RT) is a good diagnostic tool for the detection of retroviruses. We have developed a simple and rapid assay for RT activity in culture supernatants. A 370-base RNA sequence from the tetracycline-resistance gene in pBR322 plasmid DNA was used as a template for RT-mediated cDNA synthesis. To detect the resultant cDNA, we used the nested polymerase chain reaction. A sensitivity test using purified recombinant RT of human immunodeficiency virus type 1 demonstrated that the detection limit of this method was 10-7–10-8 units of RT activity in 20 μl of a test sample (2 × 10-9–2 × 10-10 units ml-1). This method detected RT activity in unconcentrated supernatants of cell cultures infected with human T-cell leukemia virus, Moloney murine leukemia virus, Moloney murine sarcoma virus, or Rous sarcoma virus. This nonisotopic method provides results within 10 h and is useful for quality control to detect retroviruses in cell cultures.
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  • 11
    ISSN: 1573-0778
    Keywords: proinsulin processing ; CHO ; mutant human proinsulin ; cell culture
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Heterologous genes encoding proproteins, including proinsulin, generally produce mature protein when expressed in endocrine cells while unprocessed or partially processed protein is produced in non-endocrine cells. Proproteins, which are normally processed in the regulated pathway restricted to endocrine cells, do not always contain the recognition sequence for cleavage by furin, the endoprotease specific to the constitutive pathway, the principal protein processing pathway in non-endocrine cells. Human proinsulin consists of B-Chain — C-peptide — A-Chain and cleavage at the B/C and C/A junctions is required for processing. The B/C, but not the C/A junction, is recognised and cleaved in the constitutive pathway. We expressed a human proinsulin and a mutated proinsulin gene with an engineered furin recognition sequence at the C/A junction and compared the processing efficiency of the mutant and native proinsulin in Chinese Hamster Ovary cells. The processing efficiency of the mutant proinsulin was 56% relative to 0.7% for native proinsulin. However, despite similar levels of mRNA being expressed in both cell lines, the absolute levels of immunoreactive insulin, normalized against mRNA levels, were 18-fold lower in the mutant proinsulin-expressing cells. As a result, there was only a marginal increase in absolute levels of insulin produced by these cells. This unexpected finding may result from preferential degradation of insulin in non-endocrine cells which lack the protection offered by the secretory granules found in endocrine cells.
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  • 12
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    Springer
    Cytotechnology 30 (1999), S. 149-158 
    ISSN: 1573-0778
    Keywords: bioreactor ; cell culture ; disposable ; wave agitation
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract This work describes a novel bioreactor system for the cultivation of animal, insect, and plant cells using wave agitation induced by a rocking motion. This agitation system provides good nutrient distribution, off-bottom suspension, and excellent oxygen transfer without damaging fluid shear or gas bubbles. Unlike other cell culture systems, such as spinners, hollow-fiber bioreactors, and roller bottles, scale-up is simple, and has been demonstrated up to 100 L of culture volume. The bioreactor is disposable, and therefore requires no cleaning or sterilization. Additions and sampling are possible without the need for a laminar flow cabinet. The unit can be placed in an incubator requiring minimal instrumentation. These features dramatically lower the purchase cost, and operating expenses of this laboratory/pilot scale cell cultivation system. Results are presented for various model systems: 1) recombinant NS0 cells in suspension; 2) adenovirus production using human 293 cells in suspension; 3) Sf9 insect cell/baculovirus system; and 4) human 293 cells on microcarrier. These examples show the general suitability of the system for cells in suspension, anchorage-dependent culture, and virus production in research and GMP applications.
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  • 13
    ISSN: 1573-0778
    Keywords: cell culture ; carcinoembryonic antigen ; aspirin ; enhanced production ; Langmuir-Blodgett film
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Medicine , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract Human colorectal adenocarcinoma tumor (CW2) cells were cultivated in RPMI 1640 media containing 0–7.5 mM aspirin and 10% fetal bovine serum for the production of carcinoembryonic antigen (CEA). By adding aspirin to the media, the production of CEA per cell increased by up to one hundred fold compared to cultivation in normal media containing no aspirin, even though the total cell concentration decreased with the increase in aspirin in the media. The production of CEA was also investigated for CW2 cells cultured on silk fibroin, poly(γ-benzyl-L-glutamate) and poly(γ-benzyl-L-glutamate)/poly(ethylene oxide) diblock copolymer films prepared by the Langmuir-Blodgett and casting methods. The highest production of CEA per cell was observed for the CW2 cells on poly(γ-benzyl-L-glutamate) and its diblock copolymer films prepared by the Langmuir-Blodgett method in the medium containing 5 mM aspirin after 168 hr of inoculation. This originates from the fact that the cell density on the films in the medium containing 5 mM aspirin was the lowest under these conditions. It is suggested that CW2 cells produce CEA more effectively when the cell growth is suppressed by addition of toxic chemicals such as aspirin or by culture on unfavorable films for cell growth.
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  • 14
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    World journal of microbiology and biotechnology 15 (1999), S. 635-637 
    ISSN: 1573-0972
    Keywords: Anthocyanin ; cell culture ; conditioned medium ; strawberry
    Source: Springer Online Journal Archives 1860-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Abstract A conditioned medium (CM) prepared from strawberry suspension cultures greatly stimulated anthocyanin accumulation. CM separated by dialysis membrane showed a significant increase (p 0.05) in anthocyanin synthesis at a fraction smaller than 10,000 Da. The stimulation by CM was eliminated when the CM was treated with alkali.
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  • 15
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 45 (1995), S. 374-378 
    ISSN: 0006-3592
    Keywords: cell culture ; patterened surfaces ; cell adhesion ; hydrogel ; polyHEMA ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Chinese hamster ovary (CHO) cells were attached to tiny adhesive sites in poly-2-hydroxyethyl methacrylate(polyHEMA-) coated glass, and their divison properties were examined. The adhesive sites were produced by placing a metal mask, containing 8-μm-diameter holes arranged in a regular pattern, on top of the coated glass and exposing the sandwich to glow discharge treatment. This treatment produced an ordered array of circular cavities in the polyHEMA down to the glass. These adhesive sites were smaller in diameter than a newborn CHO cell, so that, upon division, there would theoretically be room for only one of the two new daughter cells to remain attached. It was found that individual CHO cells attached to, and grew upon, the sites, and that division normally resulted in the releas of one of the two new daughters. It is concluded that this culture technique has applications in research on the mammalian cell cycle, cell partitioning, and cellular senescence. © 1995 John Wiley & Sons, Inc.
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  • 16
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 46 (1995), S. 147-158 
    ISSN: 0006-3592
    Keywords: CHO cell ; cell aggregation ; recombinant human interferon-γ ; mammalian cell culture ; cell culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The Chinese hamster ovary (CHO) cell line has great commercial importance in the production of recombinant human proteins, especially those for therapeutic use. Much attention has been paid to CHO cell population physiology in order to define factors affecting product fidelity and yield. Such studies have revealed that recombinant proteins, including human interferon-γ (IFN-γ), can be heterogeneous both in glycosylation and in proteolytic processing. The type of heterogeneity observed depends on the growth physiology of the cell population, although the relationship between them is complex. In this article we report results of a cytological study of the CHO320 line which expresses recombinant human IFN-γ. When grown in suspension culture, this cell line exhibited three types of heterogeneity: (1) heterogeneity of the production of IFN-γ within the cell population, (2) heterogeneity of the number of nuclei and mitotic spindles in dividing cells, and (3) heterogeneity of cellular environment. The last of these arises from cell aggregates which form in suspension culture: Some cells are exposed to the culture medium; others are fully enclosed within the mass with little or no direct access to the medium. Thus, live cells producing IFN-γ are heterogeneous in their environment, with variable access to O2 and nutrients. Within the aggregates, it appears that live cells proliferate on a dead cell mass. The layer of live cells can be several cells deep. Specific cell-cell attachments are observed between the living cells in these aggregates. Two proteins, known to be required for the formation of certain types of intercellular junctions, spectrin and vinculin, have been localized to the regions of cell-cell contact. The aggregation of the cells appears to be an active process requiring protein synthesis. © 1995 John Wiley & Sons, Inc.
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  • 17
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 46 (1995), S. 88-92 
    ISSN: 0006-3592
    Keywords: cell cycle ; hydrodynamic forces ; apoptosis ; cell culture ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Exposure of animal cells to intense hydrodynamic forces exerted in turbulent capillary flow, and by controiled agitation and aeration, resulted in preferential destruction of S and G2 cells and the extent of destruction of these cells was dependent upon the intensity of the action. The loss of these cells was possibly due to their larger size. However, the appearance of large numbers of membrane-bound vesicular structures similar to apoptotic bodies as well as cells with low DNA stainability (in a sub-G1 peak) suggested that the action of adverse hydrodynamic forces on these large cells may at least in part be to induce an apoptotic response. © 1995 John Wiley & Sons, Inc.
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  • 18
    ISSN: 0006-3592
    Keywords: one-line monitoring ; fermentation ; cell culture ; monoclonal antibodies ; real-time immunoassays ; BioCad/RPM ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: On-line, “real-time” monitoring of product concentration is important for mammalian cell culture fermentation. The continuous measurement of monoclonal antibodies allows for instantaneous determination of cell productivity and effective manipulation of the fermentor operating conditions for optimal production. This article will present the evaluation and application of a BioCad/RPM system (Per Septive Biosystems) for rapid analysis of lgG concentration for hybridoma cell cultivation. Several commercial crossflow filtration devices are tested for low protein retention and fouling properties. A protein G column is used successfully for analyzing about 400 samples of lgG1, without significant loss in separation efficiency. The Immuno Detection system is integrated into a computer-controlled 15-L fermentor. This fermentor could be operated in batch and perfusion modes with cell densities up to 20 million cells/mL. A continuous cell-free sample stream obtained by a hollow fiber filter system is introduced to the BioCad/RPM for analysis. The speed of this system allows for real-time monitoring even at high densities with fast dynamics. A murine hybridoma cell (A10G10) is cultivated in batch and continuous reactors and antibody concentration is measured continuously with complete sterility. The results are compared to offline measurements with good agreement. © 1995 John Wiley & Sons, Inc.
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  • 19
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    Biotechnology and Bioengineering 56 (1997), S. 530-537 
    ISSN: 0006-3592
    Keywords: ammonium ; cell culture ; cell cycle ; cell death ; cell growth ; Jurkat cells, GH4 cells ; LLC-PK1 cells ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The toxic effect of ammonium upon a variety of cell lines of lymphoid (Jurkat), pituitary (GH4), and renal (LLC-PK1) origin was studied. Millimolar concentrations of the ion mildly affected the growth of GH4 cells and prevented the growth of LLC-PK1 cells. The ion did not lead to the death of LLC-PK1 cells but it produced morphologic changes in these cells. The effects of ammonium upon Jurkat cells were different because cells died after accumulating at S phase. Cell death was due to apoptosis and might be related to ammonium-induced calcium mobilization from intracellular stores. These results indicate that the toxic effects caused by ammonium accumulation are different depending upon the cell type. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 530-537, 1997.
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  • 20
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    Biotechnology and Bioengineering 52 (1996), S. 166-175 
    ISSN: 0006-3592
    Keywords: bcl-2 ; apoptosis ; cell culture ; metabolic engineering ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Cell lines derived from the hemopoetic lineages are widely used as hosts for the production of biologicals. These cell lines have been demonstrated to undergo high levels of the active death program commonly referred to as apoptosis. The effects of overexpression of the apoptosis suppressor gene bcl-2 on the properties of a Burkitt lymphoma were compared with the control cell line (transfected with a negative control plasmid) under a variety of conditions relevant to cell culture production technology. In stationary batch cultures, there was a clear reduction in both the rate of total cell death and the level of apoptosis during the decline phase of the bcl-2 transfected cell cultures as compared with that of the control cell cultures. Nutrient analysis revealed that the onset of death during the control cell cultures occurred following complete exhaustion of glutamine. However, the bcl-2 transfected cell cultures continued to grow even though glutamine had been exhausted, and a significant decline in viability only occurred when glucose had also been completely exhausted.When cells were cultured in suspension without prior adaptation, the bcl-2 transfected cells grew significantly better, suggesting that the bcl-2 gene protected the cells from apoptosis triggered by either the lack of substrate or the hydrodynamic environment. Fluorescence microscopy revealed that death of the control cells was almost entirely by apoptosis, whereas death was almost exclusively by necrosis in the delayed decline phase of the transfected cell cultures. In both instances, death occurred before total exhaustion of glucose and glutamine.The induction of apoptosis following growth arrest is a major impediment to the development of culture strategies that optimize specific productivity by reducing the growth rate. Results presented here suggest that suppression of apoptosis by bcl-2 under the condition of excess thymidine allows the maintenance of cells in a growth-arrested state for much longer than would otherwise be possible.When cells were transferred to a range of commercial serum-free media, cell growth was, in all cases, much better for the bcl-2 transfected cell line. Moreover, when cells were cultivated in glutamine-free medium, the control cells exhibited a decrease in viable cell number within the first 24 h whereas, for the bcl-2 transfected cell cultures, viable cell number did not exhibit any clear decrease until after 75 h. Clearly, these results indicate that the metabolic engineering approach can be used to alter advantageously the survival and proliferative capacity of cells in cell culture environments. © 1996 John Wiley & Sons, Inc.
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  • 21
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    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 53 (1997), S. 339-344 
    ISSN: 0006-3592
    Keywords: cell culture ; tissue engineering ; thermoresponsive polymer ; cell adhesion ; insulin conjugate ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: We developed a new biomaterial for use in cell culture. The biomaterial enabled protein-free cell culture and the recovery of viable cells by lowering the temperature without the aid of supplements. Insulin was immobilized and a thermoresponsive polymer was grafted onto a substrate. We investigated the effect of insulin coupling on the lower critical solution temperature (LCST) of the thermoresponsive polymer, poly(N-isopropylacrylamide-co-acrylic acid), using polymers that were ungrafted, or coupled with insulin. The insulin conjugates were precipitated from an aqueous solution at high temperatures, but they were soluble at low temperatures. The LCST was not significantly affected by the insulin coupling. The thermoresponsive polymer was grafted to glow-discharged polystyrene film and covalently conjugated with insulin. The surface wettability of the conjugate film was high at low temperatures and low at high temperatures. The amounts of immobilized insulin required to stimulate cell growth were 1-10% of the amount of free insulin required to produce the same effect. The maximal mitogenic effect of immobilized insulin was greater than that of free insulin. About half of the viable cells was detached from the film only by lowering the temperature. The recovered cells proliferated normally on new culture dishes. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 53: 339-344, 1997.
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  • 22
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 49 (1996), S. 277-283 
    ISSN: 0006-3592
    Keywords: cell culture ; on-line viable cell concentration ; ATP balance ; redox potential ; hybridoma ; dissolved oxygen ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Two on-line methods for the estimation of viable cell number in hybridoma cultivation were investigated. One used an empirical correlation between redox potential and animal cell density. The other was based on an ATP balance with ATP steady-state assumption. Oxygen uptake rate measurement provided the amount of ATP which was produced by oxidation of NADH. Oxygen uptake rate was measured either by stationary liquid phase balance with surface aeration or by gas balance during bubble aeration with headspace flushing with an inert gas. The amount of ATP produced through the glycolysis was estimated based on the amount of lactate produced. In cultures, in which pH was controlled via manipulation of the gas phase composition, the flow of CO2 was linearly correlated with the lactate concentration. At constant dissolved oxygen levels, the viable cell density was proportional to the estimated ATP production rate, during exponential growth and during later phases. The estimated specific ATP production rate, however, varied from 2.2 pmol cell-1 h-1 at 10% air saturation to 4.5 pmol cell-1 h-1 at 100% air saturation. Specific rates of glutamine, glucose, and lactate followed the shape of the specific ATP production rate, whereas the specific oxygen uptake rate was minimal at around 50% air saturation. © 1996 John Wiley & Sons, Inc.
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  • 23
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 51 (1996), S. 466-478 
    ISSN: 0006-3592
    Keywords: optical oxygen sensor ; tissue culture flask ; cell culture ; oxygen mass transfer ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Murine hybridomas were cultivated in tissue culture flasks. Dissolved oxygen tensions in the gas and liquid phases during cell growth were monitored. Oxygen levels were measured noninvasively by interrogating an oxygen-sensitive patch mounted on the interior surface of the tissue culture flask with an optrode from outside the tissue culture flask. Readings were made in tissue culture flasks with caps both cracked open and completely closed. Although the oxygen in the gas phase remained near atmospheric oxygen levels in both flasks, over time the liquid-phase oxygen tension at the bottom of the flasks reached zero during cell growth in both the open and closed tissue culture flasks. These results suggest that the widespread practice of cracking open tissue culture flask caps during cell growth with a view to supplying adequate oxygen to cells is ineffective and probably unnecessary.The mass transfer characteristics of the tissue culture flask were also studied. The dominant resistance to oxygen mass transfer to the sensor and the cells was through the liquid media. The mass transfer rates through the liquid layer under standard laboratory conditions were found to be greater than those predicted by diffusion alone. This suggests that mixing at a microscale occurs. Volumetric and specific oxygen consumption rates were also calculated from the sensor data. These consumption rates were comparable with values published elsewhere. © 1996 John Wiley & Sons, Inc.
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  • 24
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 60 (1998), S. 689-698 
    ISSN: 0006-3592
    Keywords: purification ; cation exchange chromatography ; cell culture ; cell culture medium ; serum free ; therapeutic antibodies ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: A shortcut purification sequence for therapeutic proteins should consist of three steps: capture, purification, and polishing. Special emphasis has been put on direct capture of human monoclonal antibodies from culture supernatants with ion-exchangers avoiding pretreatment steps such as desalting, dilution, and other means to reduce the ionic strength. CM-HyperD, a cation-exchanger composed of an inorganic macroporous support filled with a viscoelastic gel with a high charge density was used. Capture of monoclonal antibodies from clarified hybridoma cell culture grown in media supplemented with fetal calf serum was investigated. Screening of different pH conditions and buffers for the load step showed that monoclonal antibodies were efficiently bound by CM-HyperD at pH 4.0 and 5.0 at an ionic strength equivalent to culture supernatant. Combination of negative purification with Q-Sepharose FF and capturing with CM-HyperD gave sufficient yield and resolution. Implementation of wash steps with higher conductivity did not improve the purity, but decreased the yield. Interestingly, high flow rates improved the purity. When antibodies were captured from serumfree culture supernatant the antibody could be eluted in a single peak with substantial reduction of contaminants. Capturing of antibodies by ion-exchange sorbents from culture supernatant is possible despite the high salt content. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 60: 689-698, 1998.
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  • 25
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 54 (1997), S. 357-364 
    ISSN: 0006-3592
    Keywords: cell culture ; hybridoma ; monoclonal antibody ; growth factor ; antigen ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The cell growth and monoclonal antibody production kinetics of hybridoma cell cultures continuously exposed to growth factors and the cognate antigen were investigated. The growth factors were the epidermal growth factor, fibroblast growth factor, and interleukin-2, whereas the antigen was the trinitrophenyl group conjugated to a carrier protein. The cultures were carried out in a protein-free medium in batch operation. During the entire cultivation period there was continuously available free, antibody-unbound antigen to interact with the cells. The produced antibody was measured with an ELISA after it was released from the antigen-protein conjugate by competitive elution with non-protein-conjugated antigen. Cultures with growth factors and without antigen increased the total antibody produced by up to 30%, whereas cell growth remained unaffacted. Soluble antigen-protein conjugates had no effect on the hybridoma cultures. In contrast, immobilized antigen-protein on sepharose beads in cultures with growth factors induced significant changes. Total antibody produced was higher by up to 40%. More importantly, the specific antibody production shifted from a growth-phase-independent to a growth-phase-dependent profile, with approximately twice as much specific antibody production during the late growth-early stationary phase relative to constant specific antibody production in the antigen-free, factor-free culture. The culture changes induced by the presence of immobilized antigen and growth factors were reversed when the antigen and the growth factors were removed from the cells' environment. © 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 357-364, 1997.
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  • 26
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 52 (1996), S. 443-448 
    ISSN: 0006-3592
    Keywords: on-line ; oxygen uptake rate ; OUR ; cell culture ; hybridoma ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Measurement of oxygen uptake rate is useful in assessing growth, viability, and metabolic activity. In cell culture, however, the oxygen demand is extremely small (typically 0.1-0.3 mM O2L-h) and is very difficult to measure accurately using conventional offgas analysis. In many industrial submerged cell culture systems, dissolved oxygen levels are controlled between preset limits by intermittent sparging of air or oxygen. This article describes a computational method for the automatic online determination of oxygen uptake from the dynamic dissolved oxygen probe response. Experimental measurements show that for a typical hybridoma culture, specific oxygen demand is 0.15 mM O2/109 cells/h. © 1996 John Wiley & Sons, Inc.
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  • 27
    ISSN: 0006-3592
    Keywords: apoptosis ; necrosis ; bcl-2 ; amino acids ; cell culture ; cell death ; hybridoma ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The transfection of murine hybridomas with the apoptosis suppressor gene bcl-2 has been reported to result in the extension of batch culture duration, leading to significant improvements in culture productivity. In the present study, the effect of deprivation, individually, of each amino acid found in culture medium was examined to characterize the chemical environment of the culture in terms of its propensity to induce apoptosis. When cells were deprived of each amino acid, individually for 48 h, the majority of cell deaths in each case occurred by apoptosis, with essential amino acids being clearly most effective. For nearly all the amino acids, the viability of the bcl-2 cell line cultures was greater than 70% after 48 h, representing a substantial improvement in viability over control cell line cultures. Time course studies revealed that the induction of death could be divided into two phases. Initially, following the deprivation of a single essential amino acid, there was a period of time during which all the control cell line cultures retained high viability. The duration of this phase varied from 15 h in the case of lysine deprivation, through to 40 h in the case methionine deprivation. In the second phase of deprivation, the cultures exhibited an abrupt and rapid collapse in viability. The time taken for the viability to fall to 50% was similar for each amino acid. In every case, the duration of both phases of the bcl-2 cultures was considerably extended. Specific utilization rates were increased during the control cultures relative to the bcl-2 cultures for both the growth phase (ranging between 2% and 57% higher than the bcl-2 cultures) and the death phase (ranging between 172% to 1900% higher than the bcl-2 culture). © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 59:90-98, 1998.
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  • 28
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 164-171 
    ISSN: 0006-3592
    Keywords: cell death ; apoptosis ; bcl -2 ; cell culture ; cell viability ; growth factors ; survival factors ; abortive proliferation ; hybridomas ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: Cultures of the CRL-1606 hybridoma (ATCC) have been reported to undergo continuous proliferation with simultaneous death during nutrient limited fed-batch fermentations. The bcl-2 proto-oncogene has been shown to prevent cell death under a variety of otherwise death inducing conditions. We were interested in elucidating the nature of the massive death observed in cultures of CRL-1606, specifically with respect to the possible environmental causes, and the ability of overexpressed human bcl-2 (hbcl-2) to mitigate cell death. Abortive proliferation, or continuous proliferation in the presence of continuous death, could be induced in serum free cultures of CRL-1606 through the withdrawal of insulin provided the culture was competent for cell proliferation. Culture competency for proliferation was found to be solely determined by the presence of cell culture nutrients. Abortive proliferation was defective in cultures transfected with hbcl-2 and the enhanced viability observed resulted from an increased viable cell population and at the expense of the nonviable cell population normally found in untransfected cultures. Abortive proliferation was also observed in serum containing cultures upon serum shiftdowns. Like the insulin-supplemented serum free culture system, hbcl-2 transfected cultures exhibited defects in the abortive proliferation process. These results suggest that the massive death observed during nutrient-limited fed-batch fermentation originate, in part, from growth or survival factor limitations. Hence, approaches to design cell culture media that account for the cell's proliferation requirements without accounting for the cell's survival requirements may represent a cell death sentence. Given the transformed nature of the hybridomas, we conclude that the abortive proliferation of CRL-1606 is a consequence of inappropriate cell cycle entry in a survival factor limited environment. © 1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 164-171, 1998.
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  • 29
    Electronic Resource
    Electronic Resource
    New York, NY [u.a.] : Wiley-Blackwell
    Biotechnology and Bioengineering 57 (1998), S. 447-453 
    ISSN: 0006-3592
    Keywords: ammonia ; cell culture ; metabolic flux ; glutamate dehydrogenase ; mass balance ; Chemistry ; Biochemistry and Biotechnology
    Source: Wiley InterScience Backfile Collection 1832-2000
    Topics: Biology , Process Engineering, Biotechnology, Nutrition Technology
    Notes: The effect of added ammonia on the intracellular fluxes in hybridoma cells was investigated by metabolic-flux balancing techniques. It was found that, in ammonia-stressed hybridoma cells, the glutamate-dehydrogenase flux is in the reverse direction compared to control cells. This demonstrates that hybridoma cells are able to prevent the accumulation of ammonia by converting ammonia and α-ketoglutarate into glutamate. The additional glutamate that is produced by this flux, as compared to the control culture, is converted by the reactions catalyzed by alanine aminotransferase (45% of the extra glutamate) and aspartate aminotransferase (37%), and a small amount is used for the biosynthesis of proline (6%). The remaining 12% of the extra glutamate is secreted into the culture medium. The data suggest that glutamate dehydrogenase is a potential target for metabolic engineering to prevent ammonia accumulation in high-cell-density culture. ©1998 John Wiley & Sons, Inc. Biotechnol Bioeng 57: 447-453, 1998.
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