Biotechnology Unit, LCDB, NIDDK, NIH, Bldg 6 Rm B1-33, Bethesda, MD, 20892, U.S.A..
Cytotechnology. 2000 Jul;33(1-3):3-11. doi: 10.1023/A:1008143132056.
The extracellular domain of human parathyroid Ca(2+) receptor was needed in order to study itsstructure and clinical application. The Ca(2+)receptor is a unique member of the G protein-coupledreceptor super-family, expressed in parathyroid andkidney cells where it has been shown to play acritical role in extracellular calcium homeostasis.The desired protein was produced by immobilizing thetransformed HEK 293 cells in a packed-bedconfiguration using a 1.6 l (working volume)bioreactor equipped with a vertical mixing impellerassembly and an internal basket. The process includeda propagation phase followed by a production phase. Inthe propagation phase, lasting approximately 160 h, the bed was perfused with a serum-containingmedium, allowing the cells to grow at a constantgrowth rate to approximately 3 x 10(10). At this point the production phase was begun, replacing themedium with serum-free medium and continuing theperfusion process for additional 350 h. Duringthis phase, the medium was pumped through the packedbed at a rate of 4-6 l per day, keeping theresidual glucose concentration around 1 g l(-1) andcollecting and processing approximately 80 l ofspent medium. This continuous perfusion method of thepacked-bed bioreactor was compared to a repeated batchmethod in which existing medium was replenished whenthe glucose concentration was down to 1 g l(-1). Using this method, serum-free medium was replaced withserum containing medium a few times when a decline inthe glucose consumption was observed. Though mediumconsumption and protein yield are similar in bothmethods (roughly 10 mg l(-1)), there aredifferences related to the ease of operation andprocessing of the produced protein. The continuousperfusion operation was found to be preferable and waschosen as the production strategy.
为了研究人甲状旁腺钙(Ca 2+)受体的结构及其临床应用,需要其细胞外结构域。Ca 2+受体是 G 蛋白偶联受体超家族的独特成员,在甲状旁腺和肾脏细胞中表达,在那里它被证明在细胞外钙稳态中发挥关键作用。所需的蛋白质是通过将转化的 HEK 293 细胞固定在填充床中,使用装有垂直混合叶轮组件和内部篮的 1.6 l(工作体积)生物反应器来生产的。该过程包括繁殖阶段和生产阶段。在繁殖阶段,持续约 160 小时,床通过含有血清的培养基进行灌注,使细胞以恒定的生长速率生长到约 3 x 10(10)。此时开始生产阶段,用无血清培养基代替培养基,并继续灌注过程 350 小时。在此阶段,将培养基以 4-6 l/天的速度泵通过填充床,将残留葡萄糖浓度保持在 1 g l(-1)左右,并收集和处理大约 80 l 用过的培养基。与补充现有培养基的重复分批方法相比,这种填充床生物反应器的连续灌注方法,当葡萄糖浓度下降到 1 g l(-1)时,会继续灌注过程。使用这种方法,当观察到葡萄糖消耗下降时,会几次用含血清的培养基代替无血清培养基。尽管两种方法的培养基消耗和蛋白质产量相似(约 10 mg l(-1)),但在操作和处理产生的蛋白质的便利性方面存在差异。连续灌注操作被发现是优选的,并被选为生产策略。