Observations consistent with autocrine stimulation of hybridoma cell growth and implications for large-scale antibody production

Existence of autocrine growth factors (aGFs) may influence the serum requirement for growth of hybridoma cells and thus significantly influence process economics. For the murine hybridoma cell line S3H5/2bA2, critical inoculum density (cID) and serum requirement for growth were inversely related for cultivation in both T flasks and spinner flasks. In spinner flasks, an inoculum density of 10⁶ cells/ml was necessary for the cells to grow in RPMI 1640 medium without serum supplement, and an inoculum density of 10³ cell/ml was necessary in RPMI 1640 medium with 10% serum. In T flasks, where the local cell density is higher than in spinner flasks, an inoculum density of 10⁶ cells/ml was necessary for the cells to grow in RPMI 1640 medium without serum supplement, and an inoculum density of 1 cell/ml was also necessary in RPMI 1640 medium with 10% serum. Further, immobilized cells at high local cell density could grow under conditions where cells in T flasks at corresponding overall cell density could not grow. The cells at high inoculum density were less sensitive to shear induced by mechanical agitation than the cells at low inoculum density. Taken together these observations support the existence of secreted aGF(s) by the hybridoma cell line used. Since the specific MAb production rate was independent of cultivation method and inoculum density, the existence of autocrine growth factors would suggest that the use of immobilized cells should improve the economics of MAb production.     

Orbital shaker technology for the cultivation of mammalian cells in suspension

For large-scale applications in biotechnology, cultivation of mammalian cells in suspension is an essential prerequisite. Typically, suspension cultures are grown in glass spinner flasks filled to less than 50% of the nominal volume. We propose a superior system for suspension cultures of mammalian cells based on orbital shaker technology. We found that "square-shaped" bottles (square bottles) provide an inexpensive but efficient means to grow HEK-293 EBNA and CHO-DG44 cells to high density. Cultures in agitated 1-L square bottles exceeded the performance of cultures in spinner flasks, reaching densities up to 7 x 10(6) cells/mL for HEK-293 EBNA cells and 5 x 10(6) cells/mL for CHO-DG44 cells in comparison to (2.5-4) x 10(6) cells/mL for cultures of the same cells grown in spinner flasks. For 1-L square bottles, optimal cell growth and viability were observed with a filling volume of 30-40% of the nominal volume and an agitation speed of 130 rpm at a rotational diameter of 2.5 cm. Transient reporter gene expression following gene delivery by calcium phosphate-DNA co-precipitation was the same or slightly better for HEK-293 EBNA cells grown in square bottles as compared to spinner flasks. Reductions in cost, simplified handling, and better performance in cell growth and viability make the agitated square bottle a new and very promising tool for the cultivation of mammalian cells in suspension.     

Olive oil addition in insect cell cultivation

Adding olive oil to an insect cell (Spodoptera frugiperda) cultivation with a TNM-FH medium enhanced cell growth. In the static cultivation, growth with 0.5% oil increased viable cell density by 32%, while cultivation in spinner flasks agitated at 260 rpm increased by 64%. With a gradual increase of agitation from 60 rpm to 500 rpm, the viable cell density was 81% higher than that without the olive oil supplement.     

人皮肤成纤维细胞在不同培养系统中的生长代谢特性

大面积烧伤病人及多种皮肤溃疡病人很难用自体皮肤移植来进行治疗.早期治疗方法采用尸体来源的皮肤移植,但由于来源有限、且有传播疾病的危险,因此应用组织工程技术构建生物活性人工皮肤已成为近十几年来在组织工程和创伤治疗领域的研究热点,目前已有几种人工皮肤成功地走向临床[1].然而,在构建大面积皮肤组织过程中,如何大量制备皮肤种子细胞仍然是一大棘手的难题,成为人体皮肤组织工程迫切需要解决的技术关键.获得大量扩增的皮肤细胞,解决种子细胞的供应问题,是构建人工皮肤的一个关键.     

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.     

Some aspects of hybridoma cell cultivation

Summary Two hybridoma cell lines were cultivated in an indirectly aerated 10-1 reactor in batch, fed-batch and continuous (perfusion) operations and in spinner flasks. The medium in the reactor was sampled either by an aseptic cross-flow filtration module integrated into a loop or by an in-situ tubular filter. The glucose concentration was monitored by an on-line flow injection analyzer and the ammonia concentration by an ion-selective electrode. Since the membrane transmission of the high-molecular components decreased during cultivation, the product, a monoclonal antibody, was enriched in the reactor. During cultivation, the concentrations of cells, viable cells, glucose, lactase, acetate, citrate, ammonia, urea, amino acids, proteins, and monoclonal antibodies were determined off-line. The specific growth rate, specific production, and consumption rates of the medium components were influenced considerably by the medium composition, especially by the type and amount of serum used.Offprint requests to: K. Schügerl     

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.     

Production of tissue plasminogen activator (tPA) in two and three dimensionally growing cultures of Bowes melanoma cells

Bowes melanoma cells synthesize more tissue plasminogen activator (tPA) in monolayer cultures than in multicell spheroids. Cellular production of tPA in these cells was measured during a cultivation period of 800 h. Without changing the cell culture assay, we were able to obtain monolayers, multilayers, and multicell spheroids (cell aggregates) by stirring microcarrier beads in 500-mL spinner flasks operated at 50 rpm. Thus, the medium conditions in the liquid were similar for cells in monolayers and in multicell spheroids. Probes for measurements of intracellular and extracellular parameters were taken from the same culture at distinct times; therefore, their variations during cultivation can directly be compared. Because cells were cultured in an unregulated (with regard to pH, glucose, etc.) spinner flask, their concentration was kept below 10(6) cells/mL, thus avoiding too fast and too severe depletion of oxygen and other medium factors. Nevertheless, the tPA productivity decreased from 8 ng/h/10(6) cells (monolayer) to 4 ng/h/10(6) cells (multicell spheroids with microcarrier nucleus, 800 mum diameter), matching the decrease of total cellular protein. Due to medium depletion, the cell cycle distribution changed from 45% to 68% G(1) cells in a characteristic way during growth of multicell spheroids. This is accompanied by changes in amino acids, glucose, lactate, and pH, which may account for the reduction of tPA productivity. (c) 1996 John Wiley & Sons, Inc.     

Investigation of the cultivation of Spodoptera frugiperda in spinner flasks and in a 10 l bioreactor with bubble-free aeration

The growth rates and attainable cell densities were compared in Grace and TC-100 media in spinner flasks of various sizes as well as in a 10-l bioreactor. In all mentioned reactors, a higher cell growth rate and final cell concentration could be obtained in the TC-100 medium than in the Grace medium. In bigger flasks, the cell concentration was higher. It was possible to maintain a constant viable cell concentration (2.45 · 10⁶ ml^–1) in continuous cultures (without perfusion) at a dilution rate of 0.01 h^–1.     

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.     

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.     

An actively mixed mini-bioreactor for protein production from suspended animal cells

Biopharmaceutical production would benefit from rapid methods to optimize production of therapeutic proteins by screening host cell line/vector combination, culture media, and operational parameters such as timing of induction. Miniaturized bioreactors are an emerging research area aiming at improving the development speed. In this work, a 3 mm thick mini-bioreactor including two 12 mm wide culture chambers connected by a 5 mm wide channel is described. Active mixing is achieved by pressure shuttling between the two chambers. Gas-liquid phase exchange for oxygen and carbon dioxide is realized by molecular diffusion through 50 microm thick polymethylpentene membranes. With this unique design, a velocity difference between the middle area and the side areas at the interfaces of the culture chambers and the connecting channel is created, which enhances the mixing efficiency. The observed mixing time is on the order of 100 s. The combination of high permeability toward oxygen of polymethylpentene membranes and fluid movement during active pressure shuttling enables higher volumetric oxygen transfer coefficients, 5.7 +/- 0.4-14.8 +/- 0.6 h(-1), to be obtained in the mini-bioreactors than the values found in traditional 50 mL spinner flasks, 2.0-2.5 h(-1). Meanwhile, the calculated volume averaged shear stress, in the range of 10(-2)-10(-1) N/m(2), is within the typical tolerable range of animal cells. To demonstrate the applicability of this mini-bioreactor to culture suspended animal cells, the insect cell, Spodoptera frugiperda, is cultured in mini-bioreactors operated under a K(L)a value of 14.8 +/- 0.6 h(-1) and compared to the same cells cultured in 50 mL spinner flasks operated under a K(L)a value of 2.2 h(-1). Sf-21 cells cultured in the mini-bioreactors present comparable length of lag phases and growth rates to their counterparts cultured in 50 mL spinner flasks, but achieve a higher maximum cell density of 5.3 +/- 0.9 x 10(6) cell/mL than the value of 3.4 +/- 0.4 x 10(6) cell/mL obtained by cells cultured in 50 mL spinner flasks. Sf-21 cells infected with SEAP-baculovirus produce a maximum SEAP concentration of 11.3 +/- 0.7 U/mL when cultured in the mini-bioreactor. In contrast, infected Sf-21 cells cultured in 50 mL spinner flasks produce a maximum SEAP concentration of 7.4 +/- 0.9 U/mL and onset of production is delayed from 18 h in minibioreactor to 40 h in spinner flasks.     

Effects of oxygen on recombinant protein production by suspension cultures of Spodoptera frugiperda (Sf-9) insect cells.

Spodoptera frugiperda (Sf-9) insect cells have been grown in serum-free medium in 250-ml spinner flasks. The maximum cell density obtained in these cultures was dependent on the aeration rate of the culture. Similar yields of uninfected cells were obtained when cultures were stirred in spinner flasks at 80 rev min-1 and in a 4-1 stirred-tank bioreactor and the dissolved oxygen in the bioreactor was controlled at 20% of air saturation. Cells were infected with a recombinant baculovirus at different multiplicities of infection: the timing and maximum level of expression of the recombinant protein were dependent on the multiplicity of infection, the cell density at infection, and on the aeration rate of the culture. Oxygen-limited growth resulted in undetectable levels of recombinant protein (< 6 ng recombinant protein 10(-7) cells). Compared with the maximum yields observed in spinner flask cultures, higher levels of recombinant protein were produced when cells were grown and infected in the bioreactor. The level of dissolved oxygen in the bioreactor was controlled at 50% of air saturation.     

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.     

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.     

Preservation of Rhizobium viability and symbiotic infectivity by suspension in water

Three Rhizobium japonicum strains and two slow-growing cowpea-type Rhizobium strains were found to remain viable and able to rapidly modulate their respective hosts after being stored in purified water at ambient temperatures for periods of 1 year and longer. Three fast-growing Rhizobium species did not remain viable under the same water storage conditions. After dilution of slow-growing Rhizobium strains with water to 10(3) to 10(5) cells ml-1, the bacteria multiplied until the viable cell count reached levels of between 10(6) and 10(7) cells ml-1. The viable cell count subsequently remained fairly constant. When the rhizobia were diluted to 10(7) cells ml-1, they did not multiply, but full viability was maintained. If the rhizobia were washed and suspended at 10(9) cells ml-1, viability slowly declined to 10(7) cells ml-1 during 9 months of storage. Scanning electron microscopy showed that no major morphological changes took place during storage. Preservation of slow-growing rhizobia in water suspensions could provide a simple and inexpensive alternative to current methods for the preservation of rhizobia for legume inoculation.     

转瓶内部结构对无血清悬浮培养昆虫细胞的影响

以昆虫细胞为宿主进行基因工程产品的开发是动物细胞培养领域十分有吸引力的研究方向[1] 。由于昆虫细胞对营养要求极高 ,且对培养环境非常敏感 ,所以一般是在含有兼具营养及保护功能的胎牛血清的培养基中进行培养。血清一方面因其高额成本而限制了昆虫细胞大规模培养技术的发展 ,另一方面又因其成分复杂、富含蛋白而给外源基因表达产物的后处理带来困难。因此 ,昆虫细胞无血清培养技术的开发一直是细胞培养工程领域的研究热点 ,采用无血清培养技术取代传统的有血清培养技术已成为昆虫细胞 杆状病毒表达系统的发展趋势[2 ] 。然而 ,昆虫细…     

Production of mosquito densonucleosis viruses by Aedes albopictus C6/36 cells adapted to suspension culture in serum-free protein-free media

Mosquito densonucleosis viruses (MDVs) have the potential for use as biocontrol agents. To facilitate densovirus production, the Aedes albopictus mosquito cell line C6/36 was adapted to two commercially available serum-free protein-free media (SFPFM), Sf-900 II and Drosophila-SFM. Cells adapted more slowly to growth in Sf-900 II medium, but once adapted, they grew more rapidly and appeared healthier than cells growing in Drosophila-SFM. Cells that were adapted to growth in each of these SFPFM were tested for their ability to be transfected and infected with MDVs. The Sf-900 II-adapted cell line survived transfection and showed infection rates comparable with cells growing in L15 supplemented with 10% fetal bovine serum. Cells adapted to Drosophila-SFM were less infectable and did not survive transfection. Cells adapted to each of these SFPFM were adapted to growth in spinner flasks. Cells in Sf-900 II grew substantially better in spinner flasks than cells in Drosophila-SFM media. Cells grown in Sf-900 II could be frozen and, when thawed, could support the production of densonucleosis viruses in spinner flasks.     

Preservation of Rhizobium viability and symbiotic infectivity by suspension in water.

Three Rhizobium japonicum strains and two slow-growing cowpea-type Rhizobium strains were found to remain viable and able to rapidly modulate their respective hosts after being stored in purified water at ambient temperatures for periods of 1 year and longer. Three fast-growing Rhizobium species did not remain viable under the same water storage conditions. After dilution of slow-growing Rhizobium strains with water to 10(3) to 10(5) cells ml-1, the bacteria multiplied until the viable cell count reached levels of between 10(6) and 10(7) cells ml-1. The viable cell count subsequently remained fairly constant. When the rhizobia were diluted to 10(7) cells ml-1, they did not multiply, but full viability was maintained. If the rhizobia were washed and suspended at 10(9) cells ml-1, viability slowly declined to 10(7) cells ml-1 during 9 months of storage. Scanning electron microscopy showed that no major morphological changes took place during storage. Preservation of slow-growing rhizobia in water suspensions could provide a simple and inexpensive alternative to current methods for the preservation of rhizobia for legume inoculation.     

用改装的Ｓuper—Spinner搅拌瓶连续灌流培养产凝血酶原ＣＨＯ工程细胞

在动物细胞培养过程中对培养体系实施培基连续灌流能及时地补充细胞生长所需的营养物质、控制细胞代谢产物对细胞的影响 ,实现细胞的高密度长期培养 ,提高目的产品的生产效率[1,2 ] 。细胞连续灌流培养的前提是在实施培基连续灌流的同时培养体系能有效地截留细胞[3] 。这一前提增加了细胞培养装置的复杂程度 ,使之特化为价格昂贵的生物反应器 ,限制了细胞连续灌流培养的应用。如能通过对普通的细胞搅拌培养瓶进行改进 ,使之能用于细胞的连续灌流培养 ,则有利于细胞连续灌流培养的推广应用。1　材料和方法1 1　细胞产人重组凝血酶原ＣＨＯ工…