Low-temperature pausing of cultivated mammalian cells

There are currently two methods for maintaining cultured mammalian cells, continuous passage at 37 degrees C and freezing in small batches. We investigated a third approach, the "pausing" of cells for days or weeks at temperatures below 37 degrees C in a variety of cultivation vessels. High cell viability and exponential growth were observed after pausing a recombinant Chinese hamster ovary cell line (CHO-Clone 161) in a temperature range of 6-24 degrees C in microcentrifuge tubes for up to 3 weeks. After pausing in T-flasks at 4 degrees C for 9 days, adherent cultures of CHO-DG44 and human embryonic kidney (HEK293 EBNA) cells resumed exponential growth when incubated at 37 degrees C. Adherent cultures of CHO-DG44 cells paused for 2 days at 4 degrees C in T-flasks and suspension cultures of HEK293 EBNA cells paused for 3 days at either 4 degrees C or 24 degrees C in spinner flasks were efficiently transfected by the calcium phosphate-DNA coprecipitation method, yielding reporter protein levels comparable to those from nonpaused cultures. Finally, cultures of a recombinant CHO cell line (CHO-YIgG3) paused for 3 days at 4 degrees C, 12 degrees C, or 24 degrees C in bioreactors achieved the same cell mass and recombinant protein productivity levels as nonpaused cultures. The success of this approach to cell storage with rodent and human cell lines points to a general biological phenomenon which may have a wide range of applications for cultivated mammalian cells.     

Surface immobilization of anchorage-dependent mammalian cells

Anchorage-dependent HeLa cells were successfully cultured on two fibrous materials (A07 and R100) with porosities of 75-125 and 40 mum, void fractions of 92% and 81%, and fiber diameters of 7.6 and 10.2 mum, respectively, in 100-mL spinner flasks and 2-L stirred tank bioreactors. The matrix was formed into a fixed vertical spiral configuration. All cultures displayed rapid (/=95%) to the matrix, uniform coverage of the immobilizing area with viable cells, and no significant amount of cell debris in the medium. Spinner flask cultures indicated that the denser material R100 showed better results in terms of final cell density. The growth of HeLa cells on material R100 in both culture systems was similar to that observed in tissue culture dishes (specific growth rate approximately 0.03-0.04 h(-1), maximum cell density of 8 x 10(6)-9 x 10(6) cells . mL(-1), and yields of 0.4 x 10(8) cells . mM(-1) on glucose and 2 x 10(8)-3 x 10(8) cells . mM(-1) on glutamine). Scale-up of this culture technique in a 2-L bioreactor under perfusion with pH and dissolved oxygen (DO) control yielded cell densities of up to 1.6 x 10(6) cells . mL(-1). Two other anchorage-dependent mammalian cells (ADC) known to be cultured with difficulty in roller bottles or with micro carriers were easily grown on material R100 in spinner flasks. The performance of this culture technique was compared to other ADC culture systems.     

Disposable orbitally shaken TubeSpin bioreactor 600 for Sf9 cell cultivation in suspension

Disposable orbitally shaken TubeSpin bioreactor 600 tubes (TS600s) were recently developed for the bench-scale cultivation of animal cells in suspension. Here we compared batch cultures of Sf9 insect cells in TS600s, spinner flasks, and shake flasks. Superior cell growth was observed in TS600s and shake flasks as compared with spinner flasks, and more favorable oxygen-enriched cell culture conditions were observed in TS600s as compared with either spinner or shake flasks. The results demonstrated the suitability of TS600s as a disposable vessel for the cultivation of Sf9 cells in suspension.     

无载体固定化培养模式下HEK293细胞的生长和代谢特征

利用HEK293细胞在悬浮培养体系中下具有聚集成团的体外培养特性,在250ml的spinner flask搅拌式细胞培养瓶中以悬浮细胞团的形式实施HEK293细胞的无载体固定化培养,以细胞密度、细胞活力、细胞团粒径分布和葡萄糖比消耗率 (qglc)、乳酸比产率 (qlac)、乳酸转化率 (Ylac/glc)、氨基酸消耗为观察指标,同时设置静止培养体系作为参照,考察无载体固定化培养模式下的HEK293细胞生长和代谢特征。观察结果表明,HEK293细胞在搅拌式细胞培养瓶中无载体固定化培养和在组织培养瓶中静止贴壁培养表现为基本相同的细胞生长和代谢特征,平均粒径小于300μm的细胞团中的物质传递能够满足HEK293细胞维持正常生长和代谢的基本需要。HEK293细胞的无载体固定化培养便于实施灌注操作、提高生物反应器单位体积的生产效率。     

Influence of culture conditions of growth of FL-74 cells and feline oncornavirus cell membrane associated antigen production.

The FL-74 cell, a feline lymphoblastoid cell line derived from a tumor induced by leukemia virus, grows equally well in static suspension culture (plastic T-flask or silicone treated glass bottles) or in spinner culture. No growth was observed in unsiliconized glass bottles. Although feline leukemia virus production was nearly the same in FL-74 grown in each of the above types of vessel, the expression of the feline oncornavirus membrane associated antigen (FOCMA), as determined by membrane immunofluorescence, was more intense and more complete on cells grown in static suspension. Moreover, higher fluorescent antibody titer endpoints were observed with cells from static suspension cultures than with cells from spinner cultures, FL-74 cells grown in spinner culture, when subjected to partial synchrony by cold block or by deprivation of essential amino acids (arginine and/or isoleucine) for 12 hr, achieved a membrane fluorescent pattern for FOCMA similar to cells grown in static suspension. It is proposed that the expression of FOCMA on the cell membrane surface is cell-cycle dependent, and that the rate at which a cell passes through the cell cycle determines the pattern and intensity of the fluorescence of the cell membrane.     

TubeSpin bioreactor 50 for the high-density cultivation of Sf-9 insect cells in suspension

Here we present the TubeSpin bioreactor 50 (TubeSpins) as a simple and disposable culture system for Sf-9 insect cells in suspension. Sf-9 cells had substantially better growth in TubeSpins than in spinner flasks. After inoculation with 10⁶ cells/ml, maximal cell densities of 16 × 10⁶ and 6 × 10⁶ cells/ml were reached in TubeSpins and spinner flasks, respectively. In addition the cell viability in these batch cultures remained above 90% for 10 days in TubeSpins but only for 4 days in spinner flasks. Inoculation at even higher cell densities reduced the duration of the lag phase. After inoculation at 2.5 × 10⁶ cells/ml, the culture reached the maximum cell density within 3 days instead of 7 days as observed for inoculation with 10⁶ cells/ml. Infection of Sf-9 cells in TubeSpins or spinner flasks with a recombinant baculovirus coding for green fluorescent protein (GFP) resulted in similar GFP-specific fluorescence levels. TubeSpins are thus an attractive option for the small-scale cultivation of Sf-9 cells in suspension and for baculovirus-mediated recombinant protein production.     

Influence of culture conditions on growth of FL-74 cells and feline oncornavirus cell membrane associated antigen production

Summary The FL-74 cell, a feline lymphoblastoid cell line derived from a tumor induced by leukemia virus, grows equally well in static suspension culture (plastic T-flask or silicone treated glass bottles) or in spinner culture. No growth was observed in unsiliconized glass bottles. Although feline leukemia virus production was nearly the same in FL-74 grown in each of the above types of vessel, the expression of the feline oncornavirus membrane associated antigen (FOCMA), as determined by membrane immunofluorescence, was more intense and more complete on cells grown in static suspension. Moreover, higher fluorescent antibody titer endpoints were observed with cells from static suspension cultures than with cells from spinner cultures. FL-74 cells grown in spinner culture, when subjected to partial synchrony by cold block or by deprivation of essential amino acids (arginine and/or isoleucine) for 12 hr, achieved a membrane fluorescent pattern for FOCMA similar to celsl grown in static suspension. It is proposed that the expression of FOCMA on the cell membrane surface is cell-cycle dependent, and that the rate at which a cell passes through the cell cycle determines the pattern and intensity of the fluorescence of the cell membrane. Supported in part by: American Cancer Society Grant IM-27 and NIH Contract NO1-CP-43217     

Transient gene expression in mammalian cells grown in serum-free suspension culture

In order to establish a simple and scaleable transfection system we have used the cationic polymer polyethylenimine (PEI) to study transient transfection in HEK293 and 293(EBNA) cells grown in serum-free suspension culture. The transfection complexes were made directly within the cell culture by consecutively adding plasmid and PEI (direct method). Alternatively, the DNA-PEI transfection complexes were prepared in fresh medium (1/10 culture volume) and then added to the cells (indirect method). The results of this study clearly show that the ratio of PEI nitrogen to DNA phosphate is very important for high expression levels. The precise ratio is dependent on the DNA concentration. For example, using 1 μg/ml DNA by the indirect method, the ratio of optimal PEI:DNA was about 10–13:1. However, the ratio increases to 33:1 for 0.1–0.2 μg/ml DNA. By testing several different molecular weights of the polycationic polymer we could show that the highest transfection efficiency was obtained with the PEI 25 kDa. Using PEI 25 kDa the indirect method is superior to the direct addition because significantly lower DNA concentrations are needed. The expression levels of the soluble human TNF receptor p55 are even higher at low DNA compared to 1 μg/ml plasmid. The EBV-based pREP vectors gave better transient gene expression when used in 293(EBNA) cells compared to HEK293 cells in suspension culture. No differences in expression levels in the two cell lines were observed when the pC1 (CMV)-TNFR was used. In conclusion, PEI is a low-toxic transfection agent which provides high levels of transient gene expression in 293(EBNA) cells grown in serum-free suspension culture. This system allows highly reproducible, cost-effective production of milligram amounts of recombinant proteins in 2–5 l spinner culture scale within 3–5 days. Fermentor scale experiments, however, are less efficient because the PEI-mediated transient tranfection is inhibited by conditioned medium. This revised version was published online in July 2006 with corrections to the Cover Date.     

Multiplexed expression and screening for recombinant protein production in mammalian cells

Background  

A variety of approaches to understanding protein structure and function require production of recombinant protein. Mammalian based expression systems have advantages over bacterial systems for certain classes of protein but can be slower and more laborious. Thus the availability of a simple system for production and rapid screening of constructs or conditions for mammalian expression would be of great benefit. To this end we have coupled an efficient recombinant protein production system based on transient transfection in HEK-293 EBNA1 (HEK-293E) suspension cells with a dot blot method allowing pre-screening of proteins expressed in cells in a high throughput manner.     

Calcium-phosphate mediated DNA transfer into HEK-293 cells in suspension: control of physicochemical parameters allows transfection in stirred media. Transfection and protein expression in mammalian cells

This is the first report of transient transfection of suspended cells with purified plasmid DNA in bioreactors or spinner flasks. DNA/calcium phosphate complexes were pumped or injected directly into stirred cultures of the immortalized human embryo kidney cell line 293 (HEK-293) which had been adapted to growth in suspension. We identified culture conditions suitable for this approach and modified the protocol for the generation of precipitate complexes, based on our earlier work. In order to stabilize the DNA-vehicle-complex in the culture medium, we identified pH ranges and ion-concentrations which prevent dissolution or aggregation of the precipitate particles. Such conditions maintained suspended fine particles in spinners or bioreactors for up to 6 hr. During that period, cells and precipitate complexes interacted sufficiently to allow DNA transfer and subsequent expression of recombinant protein. In a simple 5 day batch process, with a starting density of 0.3 × 10⁶ cells mL^-1, about 0.5 mg L^-1 of a recombinant tissue plasminogen activator variant was observed.     

Cell Culture conditions determine the enhancement of specific monoclonal antibody productivity of calcium alginate-entrapped S3H5/gamma2bA2 hybridoma cells

Immobilization offers several intrinsic advantages over free suspension cultures for the production of monoclonal antibodies. An important advantage of immobilization is the improved specific monoclonal antibody (MAb) productivity (q(MAb)) that can be obtained. However, there are conflicting reports in the literature on the enhancement of the q(MAb) with immobilization. The discrepancies between these reports can be attributed to the different to either the cultivation methods used for immobilized cell or to difference between the cell lines used in the various studies. We show that these differences may be attributed to the different cultivation methods used for one model hybridoma cell line. S3H5/Upsilon2bA2 hybridoma cells entrapped in different sizes of calcium alginate beads were cultivated in both T- and spinner flasks in order to determine whether cultivation methods (T- and spinner flasks) and bead size influence the q(MAb) Free-suspended cell cultures inoculated with cells recovered from alginate beads were also carried out in order to determine whether changes in the q(Mab) of the entrapped cells are reversible.The cultivation methods was found to influence significantly the q(MAb) of the entrapped cells. When the entrapped cells in 1-mn diameter beads were cultivated in T-flasks, the q(MAb) was not increased by 200% as previously observed in an entrapped cell culture using 1-mm-diameter alginate beads in spinner flasks. The q(MAb) of the entrapped cell was approximately 58% higher than that of the free-suspended cells in a control experiment. Unlike the cultivation method, the bead size in the range of 1- to 3-mm diameter did not significantly influence the q(MAb), regardless of cultivations methods. The changes in q(MAb) of an entrapped cells were reversible. When the free-suspended cells recovered from the T- and spinner flasks were sub-cultured in T- and spinner flasks enhanced q(MAb) of the entrapped cells in both cases decreased to the level of the free-suspended cell in a control experiments. Taken together, these results shows that the method of cultivation of hybridoma cells immobilized in alginate beads determines the extent of enhancement of the q(MAb). (c) 1993 John Wiley & Sons, Inc.     

Stirred culture of peripheral and cord blood hematopoietic cells offers advantages over traditional static systems for clinically relevant applications

The ability to culture hematopoietic cells in readily characterizable and scalable stirred systems, combined with the capability to utilize serum-free medium, will aid the development of clinically attractive bioreactor systems for transplantation therapies. We thus examined the proliferation and differentiation characteristics of peripheral blood (PB) mononuclear cells (MNC), cord blood (CB) MNC, and PB CD34(+) cells in spinner flasks and (control) T-flask cultures in both serum-containing and serum-free media. Hematopoietic cultures initiated from all sources examined (PB MNC, CB MNC, and PB CD34(+) cells) grew well in spinner vessels with either serum-containing or serum-free medium. Culture proliferation in spinner flasks was dependent on both agitator design and RPM as well as on the establishment of critical inoculum densities (ID) in both serum-containing (2 x 10(5) MNC/mL) and serum-free (3 x 10(5) MNC/mL) media. Spinner flask culture of PB MNC in serum-containing medium provided superior expansion of total cells and colony-forming cells (CFC) at high ID (1.2 x 10(6) cells/mL) as compared to T-flask controls. Serum-free spinner culture was comparable, if not superior, to that observed in serum-containing medium. This is the first report of stirred culture of PB or CB MNC, as well as the first report of stirred CD34(+) cell culture. Additionally, this is the first account of serum-free stirred culture of hematopoietic cells from any source.     

钙离子对293细胞结团和生长的影响

分别在有血清和无血清条件下、方瓶和转瓶中考察了Ca²⁺ 对2 93细胞结团和生长的影响。通过实验发现,Ca²⁺ 浓度在0 1～1 0mmol L范围内对2 93细胞的贴壁和结团性质有显著影响,而对生长影响不大。结果表明:有血清贴壁培养时,较高的Ca²⁺ 浓度有利于细胞贴壁;无血清悬浮培养中,Ca²⁺ 浓度越高,细胞结团越严重,细胞结团达到平衡后的平均粒径(D ,μm)与Ca²⁺ 浓度(c,mmol L)在0.1～0.5mmol L范围内可用一次函数D =58.65c +16.96描述,细胞结团尺寸是可调控的;而细胞在不同的Ca²⁺ 浓度下有相似的生长规律。     

Culture of insect cells in helical ribbon impeller bioreactor

An 11-L helical ribbon impeller (HRI) bioreactor was tested for the culture of Spodoptera frugiperda (Sf-9) cells. This impeller and surface baffling ensured homogeneous mixing and high oxygen transfer through surface aeration and surface-induced babble generation. Serum-supplemented and serum-free cultures, using TNMFH and IPL/41 media, respectively, grew a similar specific growth rates(0.031 and 0.028 h(-1)) to maximum cell densities of 5.5 x 10(6)-6.0 x 10(6) cells. mL(-1) with viability exceeding 98% during exponential growth phase. Growth limitation coincided with glucose and glutamine depletion and production of significant amounts of alanine. The bioreactor was further tested under more stringent conditions by infecting a serum-free medium culture with a recombinant baculovirus. Heterologous protein production of approximately 35 mug per 10(6) cells was comparable to yields obtained in serum-free cultures grown in spinner flasks and petri dishes. Average specific oxygen up-take and carbon dioxide production rates of the serum-free culture prior to infection as measured by on-line mass spectroscopy were 0.20 mumol O(2)mu.(10(6) cells)(-1) h(-1) and 0.22 mumol CO(2) . (10(6) cells)(-1)h(-1) and increased by 30-40% during infection. Therefore, the mixing and oxygenation conditions of this bioreactor were suitable for insect cell culture and recombinant protein production, with limitation being mainly attributed to nutrient depletion and toxic by-product generation.     

Transient gene expression in suspension HEK-293 cells: application to large-scale protein production

Recent advances in genomics, proteomics, and structural biology raised the general need for significant amounts of pure recombinant protein (r-protein). Because of the difficulty in obtaining in some cases proper protein folding in bacteria, several methods have been established to obtain large amounts of r-proteins by transgene expression in mammalian cells. We have developed three nonviral DNA transfer protocols for suspension-adapted HEK-293 and CHO cells: (1) a calcium phosphate based method (Ca-Pi), (2) a calcium-mediated method called Calfection, and (3) a polyethylenimine-based method (PEI). The first two methods have already been scaled up to 14 L and 100 L for HEK-293 cells in bioreactors. The third method, entirely serum-free, has been successfully applied to both suspension-adapted CHO and HEK-293 cells. We describe here the application of this technology to the transient expression in suspension cultivated HEK-293 EBNA cells of some out of more than 20 secreted r-proteins, including antibodies, dimeric proteins, and tagged proteins of various complexity. Most of the proteins were expressed from different plasmid vectors within 5-10 days after the availability of the DNA. Transfections were successfully performed from the small scale (1 mL in 12-well microtiter plates) to the 2 L scale. The results reported made it possible to establish an optimized cell culture and transfection protocol that minimizes batch-to-batch variations in protein expression. The work presented here proves the applicability and robustness of transient transfection technology for the expression of a variety of recombinant proteins.     

Semliki forest virus-based expression for versatile use in receptor research

Semliki Forest virus (SFV) vectors have been generated for highly efficient studies on gene expression in a variety of mammalian host cells, including immortalized cell lines as well as primary cells in culture. Moreover, SFV expression has been scaled up for mammalian suspension cultures in spinner flasks and bioreactors for production of large quantities of recombinant proteins for drug screening and purification. The strong preference of expression in neuronal cells in primary cell cultures, in organotypic hippocampal slices and in vivo has made SFV vectors attractive for neurobiological studies. Additionally, the engineering of novel, less cytotoxic and temperature-sensitive SFV mutant vectors has further increased their application range.     

Overexpressing human membrane proteins in stably transfected and clonal human embryonic kidney 293S cells

X-ray crystal structures of human membrane proteins, although potentially of extremely great impact, are highly underrepresented relative to those of prokaryotic membrane proteins. One key reason for this is that human membrane proteins can be difficult to express at a level, and at a quality, suitable for structural studies. This protocol describes the methods that we use to overexpress human membrane proteins from clonal human embryonic kidney 293 (HEK293S) cells lacking N-acetylglucosaminyltransferase I (GnTI(-)), and was recently used in our 2.1-? X-ray crystal structure determination of human RhCG. Upon identification of highly expressing cell lines, suspension cell cultures are scaled up in a facile manner either using spinner flasks or cellbag bioreactors, resulting in a final purified yield of ～0.5 mg of membrane protein per liter of medium. The protocol described here is reliable and cost effective, can be used to express proteins that would otherwise be toxic to mammalian cells and can be completed in 8-10 weeks.     

Improved development of human embryonic stem cell-derived embryoid bodies by stirred vessel cultivation

Human embryonic stem cells (hESCs) represent an important resource for novel cell-based regenerative medical therapies. hESCs are known to differentiate into mature cells of defined lineages through the formation of embryoid bodies (EBs) which are amenable to suspension culture for several weeks. However, EBs derived from hESCs in standard static cultures are typically non-homogeneous, leading to inefficient cellular development. Here, we systematically compare the formation, growth, and differentiation capabilities of hESC-derived EBs in stirred and static suspension cultures. A 15-fold expansion in total number of EB-derived cells cultured for 21 days in a stirred flask was observed, compared to a fourfold expansion in static (non-stirred) cultures. Additionally, stirred vessel mediated cultures have a more homogeneous EB morphology and size. Importantly, the EBs cultivated in spinner flasks retained comparable ability to produce hematopoietic progenitor cells as those grown in static culture. These results demonstrate the decoupling between EB cultivation method and EB-derived cells' ability to form hematopoietic progenitors, and will allow for improved production of scalable quantities of hematopoietic cells or other differentiated cell lineages from hESCs in a controlled environment.     

Cultivation of immortalized human hepatocytes HepZ on macroporous CultiSpher G microcarriers

Cultivation of the new immortalized hepatocyte cell line HepZ was performed with a 1:1 mixture of DMEM and Ham's F12 media containing 5% FCS. The cells were grown in their 40th passage in 100 mL and 1 L volumes in spinner flasks and in a bioreactor, respectively. For the production of adherently growing HepZ cells macroporous CultiSpher G gelatin microcarriers were used in various concentrations from 1 to 3 g/L. The cells were seeded in a density of 2 x 10(5) cells/mL when using a microcarrier concentration of 1 g/L and 5 x 10(5) cells/mL at a microcarrier concentration of 3 g/L. After 7 days of cultivation a maximum cell concentration of 4.5 x 10(6) cells/mL was obtained in the spinner culture using a microcarrier concentration of 1 g/L. With bubble-free aeration and daily medium exchange from day 7, 7.1 x 10(6) cells/mL were achieved in the bioreactor using a microcarrier concentration of 3 g/L. The cells exhibited a maximum specific growth rate of 0.84 per day in the spinner system and 1.0 per day in the bioreactor, respectively. During the growth phase the lactate dehydrogenase (LDH) activity rose slightly up to values of 200 U/L. At the end of cultivation the macroporous carriers were completely filled with cells exhibiting a spherical morphology whereas the hepatocytes on the outer surface were flat-shaped. Concerning their metabolic activity the cells predominantly consumed glutamine and glucose. During the growth phase lactate was produced up to 19.3 mM in the spinner culture and up to 9.1 mM in the bioreactor. Maximal oxygen consumption was 1950 nmol/(10(6) cells. day). HepZ cells resisted a 4-day long chilling period at 9.5 degrees C. The cytochrome P450 system was challenged with a pulse of 7 microgram/mL lidocaine at a cell density of 4.5 x 10(6) cells/mL. Five ng/mL monoethylglycinexylidide (MEGX) was generated within 1 day without phenobarbital induction compared to 26 ng/mL after a preceded three day induction period with 50 microgram/mL of phenobarbital indicating hepatic potency. Thus, the new immortalized HepZ cell line, exhibiting primary metabolic functions and appropriate for a mass cell cultivation, suggests its application for a bioartificial liver support system.     

High-density transfection with HEK-293 cells allows doubling of transient titers and removes need for a priori DNA complex formation with PEI

Recombinant proteins are of great commercial and scientific interest. Yet, most production methods in mammalian cells involve the time- and labor-consuming step of creating stable cell lines. Production methods based on transient gene expression are advantageous in terms of speed and versatility; yet, depending on the transfection protocol, transient transfection faces some bottlenecks such as a priori complex formation, limitations in terms of transfection and production media used and the need for medium exchange prior to and/or after transfection. Published protocols for transfection of suspension-adapted HEK-293 cells with polyethyleneimine have shown great promise in overcoming some of these bottlenecks, but still require a priori complex formation for optimal yields and limit the choice of transfection and production media. Here, we report successful in situ transfection of suspension-adapted HEK-293 cells with 25-kDa linear polyethyleneimine at densities up to 20 x 10(6) cells/mL in complex media followed by production at lower cell densities (1 x 10(6) cells/mL). After concentrating cells to such high densities, transfection of HEK-293 cells becomes possible in most commonly used media and is not restricted to a specific medium. Furthermore, there is no need to make transfection complexes a priori, a step that prevents inline sterile filtration of the DNA bulk for transfection, an important consideration when scaling processes up to 100 or 1,000 L. Finally, transfecting HEK-293 cells at high density in complex media is superior to existing transfection protocols and doubles yields of recombinant protein obtainable by transient gene expression.