CN113337562B - 使用CHO细胞高效发酵生产rhCG的方法 - Google Patents
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- C07K14/575—Hormones
- C07K14/59—Follicle-stimulating hormone [FSH]; Chorionic gonadotropins, e.g.hCG [human chorionic gonadotropin]; Luteinising hormone [LH]; Thyroid-stimulating hormone [TSH]
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Abstract
本申请提供了一种使用CHO细胞表达重组rhCG的补料培养发酵方法,包括在发酵混合培养基中加入氯化锰,或者在补料培养基中加入氢化可的松和焦磷酸钠。本申请还提供了所述方法用的相应培养基。
Description
技术领域
本申请属于蛋白领域和细胞培养领域,具体地,本申请提供了使用CHO细胞高效发酵生产rhCG的方法及其相应培养基。
背景技术
人绒毛膜***(hCG)由胎盘滋养细胞合成的激素,由α亚基、β亚基组成,目前广泛用于治疗女性***、性机能障碍、流产、侏儒症、皮肤瘙痒、皮痒、肿瘤等疾病。
hCG最早以孕妇尿液为原料,通过沉淀、离子交换层析等方法制备,含较多杂质、来源不确定、有传染疾病风险以及批间差异、易发生过敏反应等,在临床使用中存在风险。之后研究者把研发重点放在了利用重组技术制备和生产,并在临床上逐渐取代尿源HCG。
虽然有昆虫细胞、神经细胞等宿主的尝试,但目前rhCG生产中最常用的细胞仍然为为CHO细胞。但CHO细胞中蛋白质的表达调控机理、蛋白质翻译后修饰调控***、细胞生长代谢调控机制等环节仍然缺少深入认识,所以在外源基因的整合策略、高表达菌株的筛选、高效培养基配置、培养工艺调控等方面的理论指导水平都还比较低,相关研究都更多地依赖大量的优化筛选和优化实验来获得较优的操作条件。不仅研究和生产效率低、耗时长、成本高,而且受偶然性因素影响较大。虽然国外先进企业已经通过开发谷氨酰胺合成酶(GS)***、定制无血清个性化培养基、优化高密度微载体培养工艺和补料策略、应用低成本和低剪切力生物反应器等手段,rhCG的高水平表达仍然需要较长的培养时间(>20天)和较高的生产成本。
因此,本领域中仍然有进一步改进CHO细胞生产rhCG技术的需求。
发明内容
前期对发酵参数和细胞等因素的优化后,我们尝试了对发酵混合培养基和补料培养基的改进,研究了多种特殊添加剂对CHO表达rhCG的影响,发现在培养基中加入锰离子、氢化可的松和焦磷酸钠可以有效提高rhCG表达水平。
一方面,本申请提供了一种使用CHO细胞表达重组rhCG的补料培养发酵方法,包括在发酵混合培养基中加入氯化锰,或者在补料培养基中加入氢化可的松和焦磷酸钠。
进一步地,加入的氯化锰浓度为3mg/ml,加入的氢化可的松和焦磷酸钠浓度为0.05mg/ml和3mg/ml。
进一步地,发酵时间为12日。
进一步地,将密度1.5*106cells/ml以上的细胞接种20L到提前一夜已经预培养的50L发酵混合培养基里,接种完的当天,定为第一天,在培养第3、6、9天时分别加入10L补料培养基。
进一步地,培养参数为:36.5±1℃、pH控制在6.8-7.2、溶氧控制在20-70%,转速控制在60±5转/分。
另一方面,本申请提供了一种CHO细胞表达重组rhCG用培养基,包括发酵混合培养基和补料培养基,其中发酵混合培养基中加入了氯化锰,或者补料培养基中加入了氢化可的松和焦磷酸钠。
进一步地,加入的氯化锰浓度为3mg/ml,加入的氢化可的松和焦磷酸钠浓度为0.05mg/ml和3mg/ml。
另一方面,本申请提供了氯化锰、氢化可的松和/或焦磷酸钠在制备CHO细胞表达重组rhCG用培养基中的应用。
进一步地,培养基中氯化锰浓度为3mg/ml,氢化可的松和焦磷酸钠浓度为0.05mg/ml和3mg/ml。
附图说明
图1为CHO细胞发酵生产rhCG的基本流程。
图2为发酵培养第6日时hCG各亚基的相对丰度。
具体实施方式
实施例1发酵所用的细胞、培养基及其他试剂
发酵所用CHO细胞为申请人自制,使用LipofectamineTM2000脂质体转染试剂将携带rhCGα、β亚基的载体转染入CHO细胞K1株中制成,该细胞随后被无血清驯化并已经在申请人rhCG的试验性生产中运用超过18个月。
申请人为发酵过程配制的培养基:
传代培养基:
CD CHO AGT 24.3mg/ml、一水磷酸二氢2.69mg/ml、磷酸氢二钠4.33mg/ml、L-精氨酸550mg/ml、L-天冬酰胺1300mg/ml、L-天冬氨酸400mg/ml;
发酵混合培养基:
CD CHO AGT 24.3mg/ml、CD OPTICHO AGT 9.66mg/ml、一水磷酸二氢钠2.69mg/ml、磷酸氢二钠4.33mg/ml、生物素0.15mg/ml、叶酸11.5mg/ml、肌醇120mg/ml、氯化钾300mg/ml、葡萄糖5500mg/ml、氯化钠2100mg/ml、大豆水解蛋白30mg/ml;
补料培养基:
BalanCD CHO Feee3 66mg/ml、一水磷酸二氢钠2.69mg/ml、磷酸氢二钠4.33mg/ml、L-精氨酸2000mg/L、L-天门冬氨酸4500mg/L、维生素C15mg/L、维生素H 5mg/L叶酸30mg/L、肌醇400mg/L、维生素B12 5mg/L、氯化钾0.0015mg/L、F-68 950mg/L、葡萄糖18000mg/L;
HCG ELISA试剂盒:日本东曹;
MnCl2:济南凯创化工有限公司;
CD CHO AGT:gibco
CD OPTICHO AGT:gibco
BalanCD CHO Feee3:irvine scientific
焦磷酸钠:食品级,山东冠特生物工程有限公司;
氢化可的松:上海麦克林生化科技有限公司;
其他包括PCR试剂和仪器在内的试剂和仪器均为常规国产。
实施例2基本发酵生产过程
细胞复苏:
1)取细胞冻存管,置于37℃水浴锅内直至冻存的细胞悬液融化。
2)在吸取冻存细胞转至装有6~7ml CHO传代培养基的离心管内,离心1000rpm,5分钟,去除上清。
3)用分次吸取10mlCHO传代培养基轻轻吹打离心管内底部的成团细胞。
4)接种至装有10mlCHO传代培养基的125ml摇瓶内,使最终体积约为20ml,接种细胞密度为0.4-1.0*106个细胞/ml。将摇瓶置于二氧化碳培养箱中36.5±1℃、5±3%CO2、125±10rpm进行培养。
传代:
1)摇瓶培养:将细胞摇瓶放置于二氧化碳培养箱中36.5±1℃、5±3%CO2、125±10rpm进行培养。每天进行细胞计数,当细胞密度达到1.5*106细胞/ml以上时,进行传代,加入CHO传代培养基,调整细胞密度为0.4-1.0*106个细胞/ml。
2)wave培养:当细胞密度达1.5*106细胞/ml以上时,在把摇瓶内的细胞液收集到无菌瓶中,通过无菌接管机接种到细胞培养袋子中,调整细胞密度为0.4-1.0*106个细胞/ml,将细胞培养袋置于36.5±1℃、20±5rpm摇摆式仪上进行培养。当细胞密度达到1.5*106细胞/ml以上时,进行传代,加入CHO传代培养基,调整细胞密度为0.4-1.0*106个细胞/ml。
发酵:(100L规模):
当20L体积的细胞培养袋内细胞密度1.5*106细胞/ml以上时,接种20L到提前一夜已经预培养的50L发酵混合培养基里,接种完的当天,定为第一天,在培养第3、6、9天时分别加入10L补料培养基。培养至12天发酵结束(培养参数为:36.5±1℃、pH控制在6.8-7.2、溶氧控制在40-60%,转速控制在60±5转/分)。
发酵结束后和发酵过程中使用实施例1所述的试剂盒检测HCG水平,使用现有文献中的引物PCR检测α亚基、β亚基转录水平(α亚基:上游CTGGTCACATTGTGCTATCTTTC、下游TGAGGTGACGTTCTTTTGGAC;β亚基:上游ATGTTCCAGGGGCTGCTGCTGTT、下游CGCGGTAGTTATTGCACCACACCACCTGA)
实施例3发酵过程的优化
经过前期对发酵参数和细胞等因素的优化,我们的方法在12天时间内实现了180mg/L左右的重组蛋白的表达水平。为了进一步提高产量/在类似产量下降低成本,我们自行对定制培养基进行了进一步改进。参考现有技术,尝试向培养基中加入MnCl2(发酵混合培养基中加入3mg/ml),氢化可的松,焦磷酸钠,结果如下:
表1优化细胞株和发酵混合培养基中添加锰离子对表达水平的影响(三罐样本平均值)
进一步研究转录水平结果如图2所示:我们发现优化后的细胞株中β亚基与α亚基比率明显超过了初始细胞株,这意味着在优化后的细胞株中α亚基转录表达可能是限制产量的因素,而在发酵混合培养基中加入MnCl2可以有效提高α亚基转录水平进而提高产量;
表2补料培养基中加入氢化可的松和焦磷酸钠对表达水平的影响(优化后的细胞株,三罐样本平均值)
在补料培养基中单独加入氢化可的松或焦磷酸钠并无明显增产效果,而氢化可的松和焦磷酸钠的组合则可以实现明显提高重组蛋白表达量的效果(初步分子是补料中两者配合可以抑制细胞生长,停滞细胞周期以累积产物)。
组合锰离子、氢化可的松和焦磷酸钠后,我们在12日培养时间中实现了280.22mg/L的高表达水平。
Claims (3)
1.一种使用CHO细胞表达重组rhCG的补料培养发酵方法,其特征在于,将密度1.5*106cells/ml以上的细胞接种到发酵混合培养基里,接种完的当天,定为第一天,在培养第3、6、9天时分别加入补料培养基;补料培养基中包括浓度为0.05 mg/ml的氢化可的松和3mg/ml的焦磷酸钠。
2.根 据权利要求1所述的方法,其中发酵时间为12日。
3.根据权利要求1所述的方法,其中发酵过程中的参数为:36.5±1℃、pH控制在6.8-7.2、溶氧控制在20-70%,转速控制在60±5转/分。
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