国产生物反应器大规模高密度培养Vero细胞

本文考察了在2．5LcelliGen细胞培养器和国产20LcellCul-20细胞培养生物反应器中采用微载体技术培养细胞的情况。分析了用cellcul-20细胞培养生物反应器进行大规模培养时细胞的生长、代谢规律,研究了从2．5L扩大到20L规模的细胞转移条件。采用微载体球间直接转移技术。提高了接种效率,减少了接种步骤和污染机会。当国产GT一25微载体用量为5g／L,采用连续灌注工艺培养vero细胞,在国产20L cellCul—20细胞培养生物反应器中,连续培养5天,细胞数增加7倍,细胞密度超过1．0×10⁷ cells／m】。本文开发的细胞培养工艺,对于中试及工业规模的动物细胞大量培养具有一定的指导意义。     

大规模动物细胞培养技术研究进展

利用动物细胞大规模培养技术可生产多种生物制品,为提高细胞活力和表达水平及有利于表达产物的纯化,采用有多种添加成分的无血清培养基培养细胞,选择更有利于细胞生长又可提高培养细胞密度的微载体和条件温和、易操作、气体交换速度快的生物反应器,在线监控细胞生存环境和生理活动,减少培养过程培养基中的抑制因素,可创造更适合细胞生存的环境,提高表达水平,向细胞中导入抗凋亡基因,可提高细胞活性和蛋白产量。利用多也微载体以球转球方式大规模培养动物细胞有很好的发展前景。     

大规模动物细胞培养的问题及对策

大规模动物细胞培养在生物技术产业化进程中显示出强大的潜力。本文综述了大规模动物细胞培养过程中出现的问题及其解决办法,包括细胞培养环境、基因工程途径改建细胞系及过程监控等。对于这些进展的充分了解对优化细胞培养工艺、提高产品质量具有重要意义     

大规模动物细胞培养的问题及对策

大规模动物细胞培养在生物技术产业化进程中显示出强大的潜力。本文综述了大规模动物细胞培养过程中出现的问题及其解决办法 ,包括细胞培养环境、基因工程途径改建细胞系及过程监控等。对于这些进展的充分了解对优化细胞培养工艺、提高产品质量具有重要意义     

一种细胞培养发酵罐的评价

人和动物细胞的体外培养在生物学和医学研究中起着重要作用。然而,将动物细胞培养应用于生产却因在获得足够的产额及生物活性方面的困难而受到限制。传统上一直把细胞培养产物用作人类和牲畜的病毒疫苗,这些疫苗至今已大规模应用。在过去的七年中,大规模细胞培养技术已用于α—和β—干扰素的生产。最近,动物细胞培养技术也已用来生产大量的单克隆抗体和一些遗传工程蛋白质。     

动物细胞培养过程中的细胞凋亡

细胞培养过程中的细胞凋亡是细胞受环境因素的影响而发生的现象。随着对细胞凋亡的分子生物学和细胞生物学了解的深入,显示了有效地控制动物细胞培养中细胞凋亡的巨大潜力。包括采用ＤＮＡ重组技术把抗细胞凋亡的基因导入细胞和在培基中加入具有抗细胞凋亡的生存因子或化合物等手段已用于控制细胞培养过程中的细胞凋亡。这些技术将大大延长细胞达到饱和密度后的培养时间,提高细胞培养系统的生产效率。     

动物细胞培养过程中的细胞自然凋亡

细胞培养过程中的细胞自然凋亡是细胞受环境压力的影响而发生的现象。随着细胞自然凋亡的分子生物学和生物化学研究的深入,对以动物细胞产品生产为目的的细胞培养产业将产生极有价值的影响。采用DNA重组技术把预防细胞自然凋亡的基因导入细胞和在培基中加入具有抗细胞自然凋亡的化合物等手段已用于预防或减缓细胞培养过程中的细胞自然凋亡。这些技术将大大延长细胞达到饱和密度后的培养时间,从而使细胞培养系统的生产效率得以显著提高。     

动物细胞生物工程 第1卷

包括的内容有:一,绪论:1.引言 二、细胞培养系统的基本组成部分:2.细胞生物学——基本概念;3.细胞生物——实验;4.细胞生长培养基;5.设备消毒;6.空气消毒;。三、大量细胞培养;7.动物细胞的大批培养和产物;8.动物细胞在连续活动培养基中培养;9.单层细胞生长系统——增殖过程;10.单层细胞生长系统——异型单一过程;     

动物细胞大规模培养技术

近年来,动物细胞大规模培养技术在生物技术领域成为最受关注的热点之一,并开始广泛应用于生物医药的研发和生产过程中。以生物反应器技术为基础的动物细胞大规模培养技术平台,正逐步被建立起来并日益走向成熟,成为推动生物医药产业快速发展的有力工具。结合该技术目前的应用水平和最新进展,分析了不同细胞培养工艺之间的内在差异,以探索这一技术的未来发展方向。     

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…     

High density culture of mammalian cells with dynamic perfusion based on on-line oxygen uptake rate measurements

In a continuous culture with cell retention the perfusion rate must be adjusted dynamically to meet the cellular demand. An automated mechanism of adjusting the perfusion rate based on real-time measurement of the metabolic load of the bioreactor is important in achieving a high cell concentration and maintaining high viability. We employed oxygen uptake rate (OUR) measurement as an on-line metabolic indicator of the physiological state of the cells in the bioreactor and adjusted the perfusion rate accordingly. Using an internal hollow fiber microfiltration system for total cell retention, a cell concentration of almost 10⁸ cells/mL was achieved. Although some aggregates were formed during the cultivation, the viability remained high as examined with confocal microscopy after fluorescent vital staining. The results demonstrate that on-line OUR measurement facilitates automated dynamic perfusion and allows a high cell concentration to be achieved.     

On line estimation of oxygen uptake rate for insect cells growing in a modified spinner flask

The simple design of traditional spinner flasks makes the on-line estimation of cellular metabolism impossible. An on-line estimation system has been developed and used for the monitoring of oxygen uptake rate (OUR) for insect cells growing in a modified spinner flask. Neglect of oxygen desorption from culture media is a common source of error in OUR measurements for Sf21 cells. Therefore, an algorithm was developed to compensate for the affect of such desorption process on the determination of OUR. A modified spinner flask was successfully used as a low-volume bioreactor for insect cell cultivation and the OUR measurement developed here is both convenient and reliable.     

High viable cell concentration fed-batch cultures of hybridoma cells through on-line nutrient feeding

A hybridoma cell line was cultivated in fed-batch cultures using a low-protein, serum-free medium. On-line oxygen uptake rate (OUR) measurement was used to adjust the nutrient feeding rate based on glucose consumption, which was estimated on-line using the stoichiometric relations between glucose and oxygen consumption. Through on-line control of the nutrient feeding rate, not only sufficients were supplied for cell growth and antibody production, but also the concentrations of glucose and other important nutrients such as amino acids were maintained at low levels during the cell growth phase. During the cultivation, cell metabolism changed from high lactate production and low oxygen consumption to low lactate production and high oxygen consumption. As a result the accumulation of lactate was reduced and the growth phase was extended. In comparison with the batch cultures, in which cells reached a concentration of approximately 2 x 10(6) cells/mL, a very high concentration of 1.36 x 10(7) cells/mL with a high cell viability (>90%) was achieved in the fed-batch culture. By considering the consumption of glucose and amino acids, as well as the production of cell mass, metabolites, and antibodies, a well-closed material balance was established. Our results demonstrate the value of coupling on-line OUR measurement and the stoichiometric realations for dynamic nutrient feeding in high cell concentration fed batch cultures. (c) 1995 John Wiley & Sons, Inc.     

A comparison of different methods to determine the end of exponential growth in CHO cell cultures for optimization of scale-up

Maximizing cell growth rate and cell yield are among the most important features of a successful mammalian cell culture production process. To minimize time and resources needed to scale up cell mass it is important to maintain the cultures in exponential growth at every scale. Here we report results comparing viable cell counts, packed cell volume, intracellular nucleotide ratios, cell cycle analysis, and on-line oxygen uptake rates (OUR) and optical density for the determination of the end of exponential growth to optimize transfer times during scale-up of CHO cell cultures. Viable cell concentration, packed cell volume, and relative abundance of cells in S-phase were not very reliable at determining the end of exponential growth during the process. In contrast, on-line determination of OUR and off-line determination of intracellular nucleotide ratios (U-ratio) were very sensitive to changes in growth rate, enabling clear determination of the end of exponential growth within a short time. Although on-line OUR was found to be the most convenient and fastest method, it is restricted to instrumented and continuously monitored cultures. In contrast the nucleotide method can be applied with any culture scale and condition but needs the availability of an operator running an HPLC system and takes about an hour from sampling to result. Optical density showed an inflection along with OUR and U-ratio but was less sensitive in determining the end of exponential growth.     

On-line characterization of a hybridoma cell culture process

The on-line determination of the physiological state of a cell culture process requires reliable on-line measurements of various parameters and calculations of specific rates from these measurements. The cell concentration of a hybridoma culture was estimated on-line by measuring optical density (OD) with a laser turbidity probe. The oxygen uptake rate (OUR) was determined by monitoring dynamically dissolved oxygen concentration profiles and closing oxygen balances in the culture. The base addition for neutralizing lactate produced by cells was also monitored on-line via a balance. Using OD and OUR measurements, the specific growth and specific oxygen consumption rates were determined on-line. By combining predetermined stoichiometric relationships among oxygen and glucose consumption and lactate production, the specific glucose consumption and lactate production rates were also calculated on-line. Using these on-line measurements and calculations, the hybridoma culture process was characterized on-line by identifying the physiological states. They will also facilitate the implementation of nutrient feeding strategies for fed-batch and perfusion cultures. (c) 1994 John Wiley & Sons, Inc.     

Intracellular pH-based controlled cultivation of yeast cells: II. cultivation methodology

Intracellular pH (pH(i)) was measured on-line in a bioreactor using a fluorescent pH(i) indicator, 9-aminoacridine, and controlled fed-batch cultivations of yeast cells based on pH(i) (FB-pH(i)) were performed. In FB-pH(i) cultivations, automated glucose additions were made to the culture in response to culture pH(i). The average ethanol (an-aerobic product) yield was significantly lower [0.12 g g(-1) glucose in fed-batch pH(i) cultivations with 100 ppm glucose additions (FB-pH(i)-100 cultivation) vs. 0.48 g g(-1) glucose in batch] and cell yield was higher (0.54 g g(-1) glucose in FB-pH(i)-100 cultivation vs. 0.3 g g(-1) glucose in batch) compared to batch cultivation. An expression has been derived to calculate changes in pH(i) from measured fluorescence values when the cell concentration increases during growth. Cultivations based on pH(i), performed with different magnitudes of glucose addition (100, 50, and 10 ppm additions), showed that lower magnitudes of glucose addition resulted in lower ethanol yields while cell yield remained unaffected. The ratio of specific oxygen uptake rate to specific glucose uptake rate (OUR/GUR) increased with decreased in magnitude of glucose additions in FB-pH(i) cultivations, suggesting that the culture aerobic state was higher when the magnitude of glucose addition was lower. The average cell productivity in FB-pH(i) cultivations was 29% higher than in batch cultivation. Cells were also cultivated at high OUR conditions, and the results are compared with other cultivations. (c) 1993 John Wiley & Sons, Inc.     

杂交瘤细胞培养中摄氧速率(OUR)的在线检测及其与细胞生长及代谢的关系

在批式及灌流培养条件下研究了杂交瘤细胞在无血清培养基中的生长、代谢情况与氧消耗的关系。应用动力学方法在线进行OUR的检测,同时离线取样检测其他参数。结果发现OUR与谷氨酰胺的消耗、抗体的生成及活细胞密度间有明显的相关关系,进一步的分析还发现在对数生长期,OUR与活细胞密度间具有良好的线性关系,qOUR(0.103±0.028)×10^-12mol/cell/h,可以通过它来进行细胞密度的在线检测。并通过以ΔOUR=0时刻作为灌流调整点进行连续灌流培养的初步实验验证了OUR作为培养过程反馈控制参数的可能性。     

A new method for on-line measurement of the volumetric oxygen uptake rate in membrane aerated animal cell cultures

Oxygen is a key substrate in animal cell metabolism and its consumption is thus a parameter of great interest for bioprocess monitoring and control. A system for measuring it based on an oxygen balance on the liquid phase was developed. The use of a gas-permeable membrane offered the possibility to provide the required quantity of oxygen into the culture, while avoiding problems of foaming or shear stress generally linked to sparging. This aeration system allowed moreover to keep a known and constant k(L)a value through cultures up to 400 h. Oxygen uptake rate (OUR) was measured on-line with a very good accuracy of +/-5%, and the specific OUR for a CHO cell line was determined during batch (growth phase) and continuous culture as, respectively, equal to 2. 85x10(-13) and 2.54x10(-13) mol O(2) cell(-1) h(-1). It was also shown that OUR continuous monitoring gives actually more information about the metabolic state of the culture than the cell concentration itself, especially during transition phases like the end of the growth phase in a batch culture.     

基于活细胞量测量的利福霉素发酵过程氮源优化策略

在发酵生产利福霉素SV的过程中,其菌丝体的生长代谢情况及产物发酵合成都与有活力的菌丝量密切相关.介绍了在线活细胞传感仪测定活细胞量的方法,它利用细胞的介电特性,能够排除发酵液中固含物的干扰,测得的电容值与活细胞浓度呈线性相关,可以作为工艺优化过程中的关键参数.通过电容变化反映的前期生长出现的二次生长现象,进行了通过使用迟效氮源豆饼粉代替了原培养基中价格昂贵的速效氮源蛋白胨,成功消除了发酵前期由于氮源利用转换造成的生长停滞期,利用豆饼粉情况下培养前期的OUR和CER达到了14.8和15.3 mmol/L/h,明显高于利用速效氮源蛋白胨A组的8.6和11.3 mmol/L/h,保证了持续较高的比生长速率,对于促进菌体的氧消耗速率的增加和维持有着重要的作用,明显有利于利福霉素的合成与速率的维持,氮源替代组的发酵效价达到了5969±19 U/ml,与对照组(5030±17U/ml)相比显著提升发酵单位18.7%以上.     

Controlling the feed rate of propanol to optimize erythromycin fermentation by on-line capacitance and oxygen uptake rate measurement

The aim of the present study was to optimize the feeding proportion of glucose and propanol for erythromycin biosynthesis by real-time monitoring and exploring its limited ratio by the on-line multi-frequency permittivity measurement. It was found that the capacitance values were sensitive to the variation of biomass concentration and microbial morphology as well as the true state of cell growth. It was most favorable to both cell growth and secondary metabolism to keep the ratio of glucose to propanol at 4.3 (g/g). The specific growth rate calculated by the capacitance measurement correctly and accurately reflected the cell physiological state. An appropriate feed rate of propanol was crucial for cell growth and secondary metabolism, as well as to improve the quality of erythromycin-A. In addition, the erythromycin production titer (10,950 U/mL) was further enhanced by 4 % when the propanol feed was regulated by step-down strategy based on both OUR (oxygen uptake rate) and the on-line monitoring capacitance.