以异养细胞作为种子的椭圆小球藻产油脂光自养培养优化

异养细胞种子/光自养培养方法是一种可异养培养的能源微藻培养的有效方法,但已有文献尚未从工艺优化角度考察其发展潜力。为了获得较高细胞密度的用于光自养培养的种子和提高光自养培养的细胞密度与油脂产率,对异养细胞种子/光自养培养的培养基和培养条件进行了优化。结果表明,采用优化后的培养基,椭圆小球藻在摇瓶中异养培养的最高藻细胞密度可达11.04 g/L,比在初始培养基条件下提高了28.0%,在5 L发酵罐中异养培养的藻细胞密度达到73.89 g/L;在2 L柱式光生物反应器中光自养培养的藻细胞密度、油脂含量和油脂产率分别达1.62 g/L、36.34%和6.1 mg/(L·h),油脂成分主要为含C16-C18碳链的脂肪酸,是制备生物柴油的理想原料。经过优化,异养细胞种子/光自养培养这一方法能够显著地提高椭圆小球藻产油脂的能力,这进一步表明异养细胞种子/光自养培养方法有望成为可异养的能源微藻的高效培养方式。     

牛肾细胞在两种不同载体中培养效果的比较

目的通过牛肾细胞在两种不同载体中培养效果的比较,为牛肾细胞在细胞工厂中规模化生产提供真实的、有力的支持。方法不同代次牛肾细胞在两种载体中经过相同培养条件进行培养。结果实验中原代牛肾细胞在细胞工厂接种密度为5.5×104/cm2左右,在15 L转瓶接种密度为9.0×104/cm2左右。一代牛肾细胞在细胞工厂接种密度为6.5×104/cm2左右,在15 L转瓶接种密度为10×104/cm2左右。二代牛肾细胞在细胞工厂接种密度为7.0×104/cm2左右,在15 L转瓶接种密度为14×104/cm2左右。两种载体中牛肾细胞生长状况均能达到培养要求。结论细胞工厂能在有限的空间内利用最大限度的培养表面培养牛肾细胞,不仅节约了传代前的细胞用量,而且提高了培养后的细胞产量。     

脱色希瓦氏菌(Shewanella decolorationis) S12还原不同电子受体的厌氧发酵罐培养方法

脱色希瓦氏菌Shewanella decolorationisS12在厌氧环境下能够使用多种电子受体进行厌氧呼吸。为了取得足够的细胞量用于膜蛋白质组学等科学研究的需要,本研究选取无机小分子(硝酸钠)、金属离子(柠檬酸铁)和有机大分子(偶氮染料苋菜红)作为电子受体,在使用确定成分的无机盐培养基条件下,使用不同浓度的电子供体和碳源对S12进行厌氧条件下静置和发酵罐的优化培养,采用连续补充电子受体的培养方式,确认了电子供体和碳源的合适浓度,建立了S12厌氧发酵罐培养方法。相比传统的静置厌氧培养,厌氧发酵罐培养方法在保证了严格厌氧条件下高效率还原电子受体的同时,还极大的提高了细胞生长密度。连续补充电子受体的厌氧发酵罐培养的S12最大细胞密度最大分别可达到静置厌氧培养细胞密度的325,304,369倍,而生长时间也比静置厌氧培养分别缩短了26.5%,17.6%,7.5%。这为需要大量细胞和蛋白的细菌厌氧呼吸生长实验建立了可行方法,对于进行兼性厌氧呼吸的微生物的大规模厌氧培养具有借鉴意义。     

用昆虫细胞表达系统表达人组织激肽释放酶原

目的:利用杆状病毒-昆虫细胞表达系统表达proHUK,系统优化表达条件。方法:用改进的方法对昆虫细胞进行了无血清悬浮适应培养,用ELISA、SDS-PAGE方法对各种条件下proHUK的表达量进行检测。结果:Sf-9、Hi-5细胞在血清减量速度为5%、1%,接种密度分别为2×106cells/mL1、×106cells/mL时能很快适应无血清悬浮培养。在病毒感染复度MOI为10,细胞接种密度为1×106cells/mL条件下培养96h后,proHUK的表达量最高可达30mg/L。结论:改进的方法使昆虫细胞能更快适应无血清悬浮生长条件,获得了高表达proHUK的方法,为其大规模制备奠定了基础。     

帕米尔绿球藻的培养和条件优化

采用自养、异养、混养三种培养方式以及葡萄糖和醋酸钠两种不同的碳源对帕米尔绿球藻进行了培养。结果显示细胞在混养条件下获得了最大生物量。在异养条件下,以葡萄糖为碳源,细胞的生物量要远远高于自养条件,而以醋酸钠为碳源则结果相反。葡萄糖比醋酸钠更适合作为帕米尔绿球藻异养的碳源,5g/L的葡萄糖是比较合适的碳源浓度。     

商陆单细胞平板培养及色素高产细胞株的筛选

研究了细胞悬浮培养时间、培养方法和接种密度对商陆单细胞平板培养植板率的影响,建立了筛选色素高产细胞株的简单实用的方法。结果表明：普通单细胞平板时培养法培养商陆单细胞的植板率很低,而以悬浮培养１４－２１ｄ的单细胞为材料,接种密度为５＊１０＾３／ｍｌ时,进行条件培养和看护培养,植板率达１１．０２％。根据细胞平板培养结果,可在显微镜下直接观察单细胞克隆的颜色,筛选出商陆色素高产细胞株。     

表达重组抗CD52单克隆抗体CHO细胞灌流培养基的筛选

目的筛选重组抗CD52单克隆抗体CHO细胞株培养和连续灌流表达用培养基,以提高抗体表达量。方法通过调整原有批培养用培养基中谷氨酰胺和植物水解蛋白,获得5种培养基配比。使用模拟灌注方式进行细胞培养,分析细胞密度、活细胞比率和目标蛋白表达,筛选连续灌流细胞培养和表达用培养基。最后在7 L反应器中采用灌注培养方式对筛选获得的培养基进行验证。结果使用50 mL细胞培养管进行模拟灌注培养时,活细胞比率较高,达到90%以上;CHO细胞在添加谷氨酰胺至4.0 mmol/L和植物水解蛋白至5.0 g/L的批培养用培养基中生长速度最快;在基础培养基中抗体表达量比优化前高15%。20 d培养周期内,优化的培养基在7 L反应器中可以维持CHO细胞密度在(2 727±253)万个/mL,活细胞比率在95%以上。结论通过模拟灌注培养,筛选获得了一种在7 L反应器灌流培养中适宜于重组抗CD52单克隆抗体CHO细胞表达的培养基。     

葡萄糖对小球藻(Chloralla sp. HN08)光合作用和生长的影响

【目的】探讨葡萄糖作为外加碳源对热带海洋小球藻(Chloralla sp.HN08)生物质生产和脂、光合色素、碳水化合物及可溶性蛋白等细胞主要成份含量的影响。【方法】分析比较小球藻HN08在光合自养和兼养(添加10 g/L葡萄糖)2种营养方式下的生长速率、细胞密度、光合放氧速率、油脂相对含量,以及可溶性总糖、淀粉和可溶性蛋白的含量。【结果】结果表明,在光照条件下葡萄糖(10 g/L)能促进小球藻(Chloralla sp.HN08)生长,提高细胞终密度,而异养条件下藻细胞逐渐衰亡。兼养条件下,细胞相对生长速率及细胞终密度分别是自养条件下的6.8倍和1.3倍。兼养藻细胞中可溶性糖、淀粉、油脂含量显著高于(P0.05)光合自养细胞,然而可溶性蛋白质和光合色素含量显著低于(P0.05)光合自养细胞。添加葡萄糖的小球藻液的光饱和点和呼吸速率均高于光自养条件下的细胞,但2种培养条件下藻液的净光合速率无显著差异(P0.05)。【结论】光照条件下,添加葡萄糖可显著提高小球藻HN08相对生长速率和细胞终密度,促进油脂与淀粉的积累。     

薰衣草细胞悬浮培养体系的优化

采用正交设计方法对影响薰衣草悬浮细胞生长的因素进行了优化研究,筛选了最有利于薰衣草悬浮细胞生长的培养条件:含有0.025mg/L2,4-D、0.5mg/L6-BA、40g/L蔗糖的B5培养基和120r/min的转速,在此条件下培养15天,悬浮活细胞密度可达到4.4×105个/ml;经过3个月的培养,悬浮细胞的分化率可达到90%以上。通过分析薰衣草细胞对残糖的消耗规律,探讨了蔗糖浓度影响活细胞密度的原因。     

培养方式对真皮组织体外构建的影响

采用静态培养和转瓶培养方式分别构建真皮组织,考察培养方式和搅拌转速对细胞在三维支架材料中增殖、代谢、分布的影响。结果表明,由转瓶培养方式构建的细胞-材料复合物,其最终细胞密度和细胞比生长速率均明显高于静态培养（14.2~27.6×106 cells/cm3 vs 10.1×106 cells/cm3和0.145~0.262 d-1 vs 0.111 d-1）,而转速达80 r/min的转瓶尤其突出;静态培养的细胞-材料复合物内部细胞稀少,且分布不均匀,转瓶培养的细胞-材料复合物在材料表面和内部细胞密度都有所提高,分布情况也得到改善,且80 r/min转瓶培养的组织其细胞密度和分布均优于10 r/min和40 r/min转瓶培养。转瓶培养在其转速达到一定强度时能明显提高细胞在支架中的增殖速率,缩短培养时间,并有效改善细胞在支架内的分布,是一种理想的培养方式。     

High Yield of Human Monoclonal Antibody Produced by Stably Transfected Drosophila Schneider 2 Cells in Perfusion Culture Using Wave Bioreactor

Since it was first introduced in late 1990s Wave bioreactor has been used for protein production by mammalian and insect cell lines. However, using Wave bioreactor to produce human monoclonal antibody by stable Drosophila Schneider 2 (S2) cell transfectants has not been reported before. In this study, S2 cells were co-transfected with an inducible vector expressing human monoclonal antibody heavy and light chains, respectively, specific for hemagglutinin (HA) of H5N1 influenza virus. Stable S2 transfectant clone was selected by limiting dilution assay. Stable S2 transfectant clone that produce the highest amount of human monoclonal antibody was inoculated into two 2-l disposable cellbags, where cell growth and antibody production were compared between batch and perfusion cultures using Wave bioreactor. Here, we report that maximum viable cell density reached 1.06?×?10(7) cells/ml in batch culture; whereas 1.04?×?10(8)?cells/ml was achieved in perfusion culture. The maximum volumetric antibody productivity in batch culture was 52?mg/l/day; while perfusion culture yielded 1,437?mg/l/day. As a result, the total antibody production was 201?mg in batch culture and 8,212?mg in perfusion culture. The antibody produced by both cultures displays full neutralizing activity. Thus, our results provide strong support for using Wave bioreactor in perfusion culture for a large-scale production of human monoclonal antibody by stable S2 cell transfectants.     

Cell metabolism and medium perfusion in VERO cell cultures on microcarriers in a bioreactor

Parameters of VERO cell growth and metabolism were studied in cultures performed on microcarriers (MCs) using a bioreactor with a working capacity of 3.7?l. Kinetic studies of VERO cell growth in batch, semi-batch and perfusion cultures using concentrations of 2 and 10?mg/ml of MCs showed that a high concentration of MCs (10?mg/ml) and the use of medium perfusion allowed the attainment of higher final yields of VERO cells (6?×?10⁶ cells/ml after 10 days of culture). Perfusion also allowed better use of MCs as indicated by the observation of about 100% of MCs totally covered by cells and the appearance of multilayered cells on 64% of MCs after 13 days of VERO cell culture with 2?mg/ml of MCs. Concerning the concentration of nutrients in the cultures, the medium perfusion was able to sustain suitable levels of galactose and glutamine, which quickly decreased after 4 days in batch cultures. The air inlet in the batch cultures was capable of eliminating the NH₄ ⁺ which accumulated in the medium culture. Lactate accumulated during the first days of culture but then was utilized by the cells and decreased along the culture time. The optimization of VERO cell cultures on microcarriers as indicated by the concentration of MCs, medium perfusion and air inlet is discussed.     

单克隆抗体Mab-A生产细胞Sp2/0缩小模型培养优化研究

Sp2/0是一种生产单克隆抗体的常用细胞株。本研究首先在批次培养模式中对适合Sp2/0细胞生长的5种基础培养基、摇床转速、培养温度、二氧化碳浓度、微量元素和GlutaMAX ^TM替换谷氨酰胺等影响因素进行了筛选研究。结果显示Sp2/0细胞在批次培养中细胞密度最高值达到13.12×10 ⁶ cells/ml,培养时间为7天。除培养温度会导致不同的细胞生长密度和活率、进而影响培养时间外,其它因素不能导致明显的细胞生长差异。随后在流加培养模式下就14种补料组合进行了筛选,Sp2/0在流加培养模式下细胞的峰值密度可达20~30×10 ⁶ cells/ml,培养时间9天,单克隆抗体Mab-A日产量最高达到27.20mg/L。最后应用批次-反复流加培养模式培养Sp2/0细胞,该条件下峰值细胞数为50.42×10 ⁶ cells/ml,培养时间14天,每天单抗产量(141.10mg/L)是流加培养的5.19倍。这些研究结果为Sp2/0细胞规模化生产单克隆抗体奠定了一定基础。     

昆虫细胞(Sf21)悬浮培养过程中生长限制性基质间歇补加技术的应用

基于Sf21昆虫细胞在悬浮培养过程中所表现出的生长代谢特征,提出以培养液中残糖浓度作为控制参数,并利用限制性基质(葡萄糖和蛋白水解物)的间歇补加技术调控细胞生长的方案。实际控制表明：与批培养相比,Sf21细胞在两种具代表性的昆虫细胞培养基(IPL-41和TC-100)中的生长期和稳定期都得到了有效的延长。TC-100培养液中最高细胞培养密度由3.0×10⁶ cells/mL提高到6.5×10⁶ cells/mL;IPL41培养液中最高细胞培养密度则由7.05×10⁶ cells/mL提高到9.0×10⁶cells/mL。由于限制性基质的间歇补加技术是利用较确定的营养成分来代替复杂昂贵的补料培养基,因此更适合于昆虫细胞的大规模高密度培养。     

Effect of culture temperature on follicle-stimulating hormone production by Chinese hamster ovary cells in a perfusion bioreactor

Follicle-stimulating hormone (FSH) was produced in Chinese hamster ovary (CHO) cells using a perfusion bioreactor. Perfusion culture at 37°C yielded a high cell density but a low FSH production. To investigate the effect of culture temperature in the range of 26–37°C on cell growth and FSH production, batch cultures were performed. Lowering culture temperature below 32°C resulted in growth suppression. However, specific productivity of FSH, q _FSH, increased as culture temperature decreased, and the maximum q _FSH of 43.4 ng/10⁶ cells/h was obtained at 28°C, which is 13-fold higher than that at 37°C. Based on the results obtained from batch cultures, we performed perfusion cultures with two consecutive temperatures. CHO cells were grown up to 3.2 × 10⁷ cells/ml at 37°C and culture temperature shifted down to 28°C to obtain a high FSH titer. Soon after the maximum FSH titer of 21 μg/ml was achieved, a rapid loss of not only viable cell concentration but also cell viability was observed, probably due to the low activities of enzymes related to cell growth. Thus, the extension of production period at 28°C is critical for the enhancement of FSH production, and the use of antiapoptotic genes seems to be promising.     

High density VERO cell culture on microcarriers in a cell bioreactor

VERO cells were cultivated in microcarriers (MCs) using a bioreactor with a working capacity of 3.7 l. We studied the effect of MCs concentration in the proportion of MC-bearing cells and on the kinetics of cell growth, as well as the cell growth with a batch, fed-batch and perfusion mode operation. The data show that, in a batch system, with an initial VERO cell inoculum of 3×10⁴ cells/mg of MCs, 65%, 55% and 50% of the MCs were shown to be totally covered by cells after 7 days in cultures with respectively 2, 5 and 10 mg/ml of MCs. It was observed, that higher concentrations of MCs produced higher final yields of VERO cells. With 10 mg/ml of MCs, after 7 days of culture, a final yield of 10¹⁰ cells in the bioreactor, was obtained. The study of cell growth with a batch, fed-batch or perfusion system showed that the medium renewal allowed the continuous cell growth with the obtention of a final yield of 4×10⁹ cells in a culture with 2 mg/ml of MCs. The number of cells that can be easily reached in these culture systems, which can be even further improved, indicates its usefulness for cell propagation and the preparation of cell products such as viral antigens.This work was supported in part by grants from the Fundação de Amparo à Pesquisa do Estado de S. Paulo (FAPESP), Fundação Instituto Butantan, and European Economic Community (EEC). C.A. Pereira is recipient of a Conselho Nacional de Pesquisa (CNPq) fellowship. We thank A.C. Barbosa for technical assistance.     

Production of recombinant h-AT III with mammalian cell cultures using capillary electrophoresis for product monitoring

The importance of mammalian cell cultures for biotechnological production processes is steadily increasing, despite the high demands of these organisms on their culture conditions. Efforts towards a more efficient bioprocess generally concentrate on maximizing the culture's life time, the cell number, and the product concentration. Here recombinant BHK 21 c13 cells are used to produce rh-AT III, an anticoagulant of high therapeutic value. The influence of the process mode (batch, repeated batch, continuous perfusion) and the process temperature (30°C vs. 37°C) on the above mentioned parameters is investigated. It is possible to increase the length of the culture from 140 h (batch) to more than 500 h (continuous perfusion culture), while concomitantly increasing the cell density from 0.72 10⁶/ml (batch) to 2.27 10⁶/ml (repeated batch) and 2.87 10⁶/ml (continuous perfusion culture). The accumulation of toxic metabolites, such as lactate, can be curtailed by reducing the bioreactor temperature from 37°C to 30°C during the later part of the exponential growth phase. Fast and reliable product monitoring became essential during process optimization. Capillary zone electrophoresis (CZE) in uncoated fused silica capillaries was studied for that purpose and compared to the standard ELISA. Under optimized conditions an AT III quantification could be done within 2 min with CZE. The detection limit was 5 g/ml. A relative standard deviation of less than 0.9% was calculated. The detection limit could be lowered by one order of magnitude by using a two dimensional system, where an liquid chromatographic (LC) system is coupled to the CZE. Concomitantly the resolution is improved. The two-dimensional analysis required 5 min. Membrane adsorbers (MA) were used as stationary phase in the LC-system, to allow the application of high flow rates (5–10 ml/min). The correlation between the LC-CZE analysis and the standard AT III-ELISA was excellent, with r²: 0.965. Using the assay for at line product monitoring, it is shown, that the process temperature is of no consequence for the productivity whereas the process mode strongly influences this parameter.     

Hydrocyclones as cell retention device for CHO perfusion processes in single-use bioreactors

In this study, a hydrocyclone (HC) especially designed for mammalian cell separation was applied for the separation of Chinese hamster ovary cells. The effect of key features on the separation efficiency, such as type of pumphead in the peristaltic feed pump, use of an auxiliary pump to control the perfusate flow rate, and tubing size in the recirculation loop were evaluated in batch separation tests. Based on these preliminary batch tests, the HC was then integrated to 50-L disposable bioreactor bags. Three perfusion runs were performed, including one where perfusion was started from a low-viability late fed-batch culture, and viability was restored. The successive runs allowed optimization of the HC-bag configuration, and cultivations with 20–25 days duration at cell concentrations up to 50 × 10⁶ cells/ml were performed. Separation efficiencies up to 96% were achieved at pressure drops up to 2.5 bar, with no issues of product retention. To our knowledge, this is the first report in literature of high cell densities obtained with a HC integrated to a disposable perfusion bioreactor.     

Performance of small-scale CHO perfusion cultures using an acoustic cell filtration device for cell retention: characterization of separation efficiency and impact of perfusion on product quality

Several small-scale Chinese hamster ovary (CHO) suspension cultures were grown in perfusion mode using a new acoustic filtration system. The separation performance was evaluated at different cell concentrations and perfusion rates for two different CHO cell lines. It was found that the separation performance depends inversely on the cell concentration and perfusion rate. High media flow rates as well as high cell concentrations resulted in a significant drop in the separation performance, which limited the maximal cell concentration achievable. However, packed cell volumes of 10% to 16% (corresponding to 3 to 6. 10(7) cells/mL) could be reached and were maintained without additional bleeding after shifting the temperature to 33 degrees C. Perfusion, up to 50 days, did not harm the cells and did not result in a loss of performance of the acoustic filter as often seen with other perfusion systems. Volumetric productivities in perfusion mode were 2- to 12-fold higher for two cell lines producing two different glycoproteins when compared to fed-batch or batch processes using the same cell lines. Product concentrations were in the range of 20% to 80% of batch or fed-batch culture, respectively. In addition, using the protease-sensitive product rhesus thrombopoietin, we could show that cultivation in perfusion mode drastically reduced proteolysis when compared to a batch culture without addition of protease inhibitors such as leupeptin.     

Bioprocess development for the production of mouse-human chimeric anti-epidermal growth factor receptor vIII antibody C12 by suspension culture of recombinant Chinese hamster ovary cells

The mouse-human chimeric anti-epidermal growth factor receptor vIII (EGFRvIII) antibody C12 is a promising candidate for the diagnosis of hepatocellular carcinoma (HCC). In this study, 3 processes were successfully developed to produce C12 by cultivation of recombinant Chinese hamster ovary (CHO-DG44) cells in serum-free medium. The effect of inoculum density was evaluated in batch cultures of shaker flasks to obtain the optimal inoculum density of 5 × 10⁵ cells/mL. Then, the basic metabolic characteristics of CHO-C12 cells were studied in stirred bioreactor batch cultures. The results showed that the limiting concentrations of glucose and glutamine were 6 and 1 mM, respectively. The culture process consumed significant amounts of aspartate, glutamate, asparagine, serine, isoleucine, leucine, and lysine. Aspartate, glutamate, asparagine, and serine were particularly exhausted in the early growth stage, thus limiting cell growth and antibody synthesis. Based on these findings, fed-batch and perfusion processes in the bioreactor were successfully developed with a balanced amino acid feed strategy. Fed-batch and especially perfusion culture effectively maintained high cell viability to prolong the culture process. Furthermore, perfusion cultures maximized the efficiency of nutrient utilization; the mean yield coefficient of antibody to consumed glucose was 44.72 mg/g and the mean yield coefficient of glutamine to antibody was 721.40 mg/g. Finally, in small-scale bioreactor culture, the highest total amount of C12 antibody (1,854 mg) was realized in perfusion cultures. Therefore, perfusion culture appears to be the optimal process for small-scale production of C12 antibody by rCHO-C12 cells.