CN114990077A - Lentiviral packaging and purification method - Google Patents

Lentiviral packaging and purification method Download PDF

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CN114990077A
CN114990077A CN202210915387.8A CN202210915387A CN114990077A CN 114990077 A CN114990077 A CN 114990077A CN 202210915387 A CN202210915387 A CN 202210915387A CN 114990077 A CN114990077 A CN 114990077A
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谢海涛
方晓
马丽雅
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Shenzhen Xiankangda Life Science Co ltd
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Description

一种慢病毒包装与纯化方法A kind of lentivirus packaging and purification method

技术领域technical field

本发明涉及细胞培养技术,尤其涉及一种慢病毒包装与纯化方法。The invention relates to cell culture technology, in particular to a lentivirus packaging and purification method.

背景技术Background technique

随着免疫治疗产业的发展,越来越多的研究机构、医药公司投身于CAR-T的研发、临床试验和产业化制备。CAR-T全称嵌合抗原受体T细胞(Chimeric Antigen Receptor T-Cell Immunotherapy,CAR-T),是一种利用基因工程的方法设计、合成CAR基因,通过慢病毒载体转入T细胞,从而得到CAR-T细胞,回输给患者。目前,国外和国内已经有CAR-T产品上市,并且还有很多的临床试验正在进行,可以说,CAR-T治疗很有可能开发出治愈肿瘤的细胞治疗方案,造福人类。With the development of the immunotherapy industry, more and more research institutions and pharmaceutical companies have devoted themselves to the research and development, clinical trials and industrialized preparation of CAR-T. The full name of CAR-T is Chimeric Antigen Receptor T-Cell Immunotherapy, CAR-T. It is a kind of CAR gene designed and synthesized by genetic engineering, and transferred into T cells by lentiviral vector, so as to obtain CAR-T. CAR-T cells are infused back into the patient. At present, CAR-T products have been launched in foreign and domestic markets, and many clinical trials are underway. It can be said that CAR-T therapy is likely to develop a tumor-curing cell therapy program for the benefit of mankind.

慢病毒具有转导效率高、可整合T细胞基因组并持续表达目标蛋白等优势,是转染、电转、逆转录病毒、腺病毒等无法比拟的优势。现如今,CAR-T细胞的临床研究及上市产品的生产大多基于慢病毒载体介导的CAR基因转移,因此,慢病毒必须符合GMP标准。Lentivirus has the advantages of high transduction efficiency, integration of T cell genome and continuous expression of target protein, etc. It is an incomparable advantage of transfection, electroporation, retrovirus, adenovirus, etc. Nowadays, most of the clinical research of CAR-T cells and the production of marketed products are based on lentiviral vector-mediated CAR gene transfer. Therefore, lentiviruses must meet GMP standards.

当前,慢病毒的制备生产分为两种,一种贴壁细胞包装制备,一种悬浮细胞包装制备。贴壁细胞包装制备慢病毒的工艺大多基于依赖胎牛血清(FBS)的贴壁细胞工艺,其具有慢病毒表达滴度高、硬件投入少等优点;然而,依据GMP标准,用于人体的生物制品必须不含动物源性成分,其依赖胎牛血清,这与当前的法规不相适宜。如使用胎牛血清进行慢病毒的制备,将会大大增加下游纯化设备、耗材、试剂的成本。悬浮细胞包装制备慢病毒的工艺,先将293T细胞训化成不依赖胎牛血清的细胞,但是训化过程繁琐,训化后的细胞在慢病毒包装的过程中状态不佳,同时,包装过程中需要投入大量的设备成本,需要更大的人力物力财力成本,对企业的发展增加过大的负担。At present, the preparation and production of lentiviruses are divided into two types, one for adherent cell packaging and the other for suspension cell packaging. Most of the processes for the preparation of lentivirus by adherent cell packaging are based on the adherent cell process relying on fetal bovine serum (FBS), which has the advantages of high lentiviral expression titer and low hardware investment; Products must be free of animal-derived components, which rely on fetal bovine serum, which is incompatible with current regulations. If fetal bovine serum is used for lentivirus preparation, the cost of downstream purification equipment, consumables and reagents will be greatly increased. In the process of preparing lentivirus by suspension cell packaging, 293T cells are first trained into cells that do not depend on fetal bovine serum, but the training process is cumbersome, and the trained cells are in poor condition during the lentivirus packaging process. It needs to invest a lot of equipment costs, and requires greater human, material, and financial costs, which increases an excessive burden on the development of the enterprise.

发明内容SUMMARY OF THE INVENTION

基于上述问题,本发明所要解决的问题在于提供一种纯化难度小、成本低,且无动物源性成分带入的慢病毒包装与纯化方法。Based on the above problems, the problem to be solved by the present invention is to provide a lentivirus packaging and purification method with low purification difficulty, low cost, and no animal-derived components.

本发明的技术方案如下:The technical scheme of the present invention is as follows:

一种慢病毒包装与纯化方法,包括如下步骤:A lentivirus packaging and purification method, comprising the following steps:

将处于对数生长期的293T细胞采用完全培养基重悬后转入细胞工厂,静置培养;The 293T cells in logarithmic growth phase were resuspended in complete medium and transferred to the cell factory for static culture;

静置培养24小时后,去掉完全培养基,加入无血清培养基,继续孵育;After standing for 24 hours, remove the complete medium, add serum-free medium, and continue to incubate;

将四质粒、PEI和OPTI-MEM混合均匀后进行孵育,随后补充加入无血清培养基,得到质粒转染混合液;The four plasmids, PEI and OPTI-MEM were mixed evenly and incubated, and then supplemented with serum-free medium to obtain a plasmid transfection mixture;

细胞工厂孵育293T细胞完成后去掉无血清培养基,接着往所述细胞工厂加入所述质粒转染混合液,进行转染处理;After incubating the 293T cells in the cell factory, remove the serum-free medium, and then add the plasmid transfection mixture to the cell factory for transfection;

转染处理结束后,去掉所述质粒转染混合液,并加入全新的无血清培养基,静置培养;静置培养过程中,收集慢病毒上清液;After the transfection treatment, the plasmid transfection mixture was removed, and a new serum-free medium was added for static culture; during the static culture, the lentivirus supernatant was collected;

对慢病毒上清液依次进行Q膜富集、核酸酶酶解、离子交换处理后,获得慢病毒纯化液;The lentivirus supernatant was sequentially subjected to Q membrane enrichment, nuclease enzymatic hydrolysis and ion exchange treatment to obtain a lentivirus purified solution;

所述慢病毒纯化液依次进行浓缩、过滤,获得纯化的慢病浓缩液,然后分装、冻存、备用。The lentivirus purified solution is successively concentrated and filtered to obtain a purified chronic disease concentrate, which is then packaged, frozen, and used for later use.

一实施例,所述慢病毒包装与纯化方法中,所述293T细胞转入细胞工厂时:293T细胞的转入量为5.0×108~10.0×108;所述细胞工厂为十层细胞工厂;且所述完全培养基为含10%(v/v)FBS的完全培养基;优选,所述293T细胞转入细胞工厂时:293T细胞的转入量为8.0×108In one example, in the lentivirus packaging and purification method, when the 293T cells are transferred into a cell factory: the transfer amount of the 293T cells is 5.0×10 8 to 10.0×10 8 ; the cell factory is a ten-layer cell factory and the complete medium is a complete medium containing 10% (v/v) FBS; preferably, when the 293T cells are transferred into the cell factory: the transfer amount of the 293T cells is 8.0×10 8 .

一实施例,所述慢病毒包装与纯化方法中,所述293T细胞静置培养停止后,所述无血清培养基的加入量为500~700ml,且孵育时间为1小时;优选,所述293T细胞静置培养停止后,所述无血清培养基的加入量为625ml。In one embodiment, in the lentivirus packaging and purification method, after the stationary culture of the 293T cells is stopped, the serum-free medium is added in an amount of 500-700 ml, and the incubation time is 1 hour; preferably, the 293T After the stationary culture of cells was stopped, the added amount of the serum-free medium was 625 ml.

一实施例,所述慢病毒包装与纯化方法中,所述质粒转染混合液制备步骤中, PEI与四质粒总数按2:1(v/m);所述孵育时间为10~30分钟;优选,所述孵育时间为20分钟。In one embodiment, in the lentivirus packaging and purification method, in the preparation step of the plasmid transfection mixture, the total number of PEI and the four plasmids is 2:1 (v/m); the incubation time is 10-30 minutes; Preferably, the incubation time is 20 minutes.

一实施例,所述慢病毒包装与纯化方法中,所述质粒转染处理步骤中,转染处理时间为5~7小时;优选,转染处理时间为6小时。In one embodiment, in the lentivirus packaging and purification method, in the plasmid transfection treatment step, the transfection treatment time is 5-7 hours; preferably, the transfection treatment time is 6 hours.

一实施例,所述慢病毒包装与纯化方法中,所述质粒转染处理结束后,加入全新的所述无血清培养基的量为1000~1400ml;优选,所述无血清培养基的加入量为1250ml。In one embodiment, in the lentivirus packaging and purification method, after the plasmid transfection treatment is completed, the amount of the new serum-free medium added is 1000-1400 ml; preferably, the amount of the serum-free medium added is 1250ml.

一实施例,所述慢病毒包装与纯化方法中,所述慢病毒上清液的收集时间分别是在静置培养的第24小时和第48小时。In one embodiment, in the lentiviral packaging and purification method, the lentiviral supernatant is collected at the 24th hour and the 48th hour of static culture, respectively.

一实施例,所述慢病毒包装与纯化方法中,所述慢病毒上清液处理步骤中,所述Q膜采用的是Mustang Q XT5;离子交换处理中使用的离子交换层析柱的填料为Sepharose4FF。In one embodiment, in the lentivirus packaging and purification method, in the lentivirus supernatant processing step, the Q membrane is Mustang Q XT5; the ion exchange chromatography column filler used in the ion exchange treatment is Sepharose4FF.

一实施例,所述慢病毒包装与纯化方法中,所述慢病毒纯化液浓缩的过滤处理还包括:浓缩后的慢病毒,加入终浓度为10%(v/v)的人血白蛋白和终浓度为5%(v/v)的蔗糖水溶液,混合均匀后,再用0.22滤膜无菌过滤。In one embodiment, in the lentivirus packaging and purification method, the filtration treatment for the concentration of the lentivirus purified solution further comprises: adding the concentrated lentivirus with a final concentration of 10% (v/v) human albumin and A sucrose aqueous solution with a final concentration of 5% (v/v) was mixed uniformly, and then sterile filtered through a 0.22 membrane filter.

与现有技术相比,本发明具有如下优点:Compared with the prior art, the present invention has the following advantages:

1 )、本发明在慢病毒包装前,293T用10%FBS完全培养基培养,处于对数期的293T细胞处于最佳的状态,保证慢病毒包装过程中的细胞状态,同时保证了慢病毒的高滴度;1), in the present invention, before lentivirus packaging, 293T is cultured with 10% FBS complete medium, and the 293T cells in log phase are in the best state, ensuring the cell state during the lentivirus packaging process, and at the same time ensuring the lentivirus. high titer;

2 )、本发明在慢病毒包装的过程中,完全使用无血清培养基,使下游纯化更简单,更容易获得符合GMP标准的慢病毒;2), in the process of lentivirus packaging, the present invention completely uses serum-free medium, which makes downstream purification simpler and easier to obtain lentiviruses that meet GMP standards;

3)、本发明在慢病毒包装的过程中,控制293T细胞的数量,使细胞在包装的过程中保持在最好的状态;3) In the process of lentivirus packaging, the present invention controls the number of 293T cells to keep the cells in the best state during the packaging process;

4)、本发明在慢病毒纯化中,采用Q膜富集、核酸酶酶解,离子交换,浓缩后即得到符合GMP要求的慢病毒,工艺简单,成本低;4) In the lentivirus purification of the present invention, Q membrane enrichment, nuclease enzymatic hydrolysis, and ion exchange are used to obtain lentiviruses that meet GMP requirements after concentration, the process is simple, and the cost is low;

本发明在慢病毒的包装过程中用无血清培养基,使293T细胞在包装过程中保持状态的同时,不带入动物源性成分,使下游的慢病毒纯化更简单;即保证了慢病毒的滴度,减少设入成本的同时,更高效地获得符合GMP标准的慢病毒。In the present invention, serum-free medium is used in the lentivirus packaging process, so that the 293T cells are kept in the state during the packaging process, and animal-derived components are not introduced, so that the downstream lentivirus purification is simpler; that is, the lentivirus is guaranteed. titer, reduce the cost of installation, and obtain GMP-compliant lentivirus more efficiently.

附图说明Description of drawings

图1为本发明提供的慢病毒包装与纯化工艺流程图;Fig. 1 is the lentivirus packaging and purification process flow chart provided by the present invention;

图2、3、4、5分别为对比例1、实施例1至3对应慢病毒包装过程中FBS对纯化峰图的影响;Figures 2, 3, 4, and 5 are the effects of FBS on the purification peaks during the corresponding lentivirus packaging process of Comparative Example 1 and Examples 1 to 3, respectively;

图6为293T细胞包装数量对慢病毒滴度的影响。Figure 6 shows the effect of 293T cell packaging number on lentivirus titers.

具体实施方式Detailed ways

下面结合附图,对本发明的较佳实施例作进一步详细说明。The preferred embodiments of the present invention will be described in further detail below with reference to the accompanying drawings.

如图1所示,本发明提供的一种慢病毒包装及纯化方法,包括如下工艺步骤:As shown in Figure 1, a kind of lentivirus packaging and purification method provided by the present invention comprises the following process steps:

S1、将处于对数期的5.0×108~10.0×108个293T细胞采用完全培养基重悬后转入细胞工厂,静置培养;S1. 5.0×10 8 ~10.0×10 8 293T cells in log phase were resuspended in complete medium and transferred to the cell factory for static culture;

S2、静置培养24小时后,弃掉细胞工厂中的完全培养基,加入500~700ml无血清培养基,孵育1小时;转步骤S4;S2. After 24 hours of static culture, discard the complete medium in the cell factory, add 500-700ml of serum-free medium, and incubate for 1 hour; go to step S4;

S3、将四质粒及PEI与OPTI-MEM混合均匀,孵育10~30分钟后补无血清培养基至625ml,得到质粒转染混合液;转步骤S4;S3. Mix the four plasmids, PEI and OPTI-MEM evenly, incubate for 10-30 minutes, and then add serum-free medium to 625ml to obtain a plasmid transfection mixture; transfer to step S4;

S4、步骤S2中的十层细胞工厂孵育完成后,弃掉所述无血清培养基,再加入步骤S3中的质粒转染混合液,转染处理5~7小时;S4. After the incubation of the ten-layer cell factory in step S2 is completed, the serum-free medium is discarded, and the plasmid transfection mixture in step S3 is added, and the transfection is processed for 5-7 hours;

S5、转染处理结束后,弃掉质粒转染混合液,加入1000~1400ml无血清培养基;S5. After the transfection treatment, discard the plasmid transfection mixture and add 1000~1400ml of serum-free medium;

S6、分别在第24h和第48h收集慢病毒上清;S6, collect lentiviral supernatant at 24h and 48h respectively;

S7、对收集的慢病毒上清依次进行Q膜富集、核酸酶酶解、离子交换处理,获得慢病毒纯化液;S7, performing Q membrane enrichment, nuclease enzymatic hydrolysis, and ion exchange treatment on the collected lentivirus supernatant in sequence to obtain a lentivirus purified solution;

S8、将慢病毒纯化液进行超滤浓缩、无菌过滤后,得到慢病毒浓缩液;S8, the lentivirus purified solution is subjected to ultrafiltration concentration and sterile filtration to obtain a lentivirus concentrate;

S9、慢病毒浓缩液分装、冻存,即得到纯化的慢病毒制剂。S9, the lentivirus concentrate is divided into packs and frozen to obtain a purified lentivirus preparation.

上述步骤中,步骤S1-S4为慢病毒包装过程;而步骤S5-S9为慢病毒的收集与纯化过程。In the above steps, steps S1-S4 are lentivirus packaging processes; and steps S5-S9 are lentivirus collection and purification processes.

进一步的方案是,所述步骤S1中,293T细胞的数量为8.0×108,293T细胞先用含10%FBS(胎牛血清)的完全培养基重悬后,再转入十层细胞工厂中。A further scheme is that in the step S1, the number of 293T cells is 8.0×10 8 , and the 293T cells are first resuspended in a complete medium containing 10% FBS (fetal bovine serum), and then transferred to a ten-layer cell factory. .

进一步的方案是,所述步骤S1中,完全培养基中含10v/v%FBS(胎牛血清),可以保证293T在慢病毒包装前处于最佳状态;细胞工厂采用十层细胞工厂。A further scheme is that, in the step S1, the complete medium contains 10v/v% FBS (fetal bovine serum), which can ensure that 293T is in the best state before lentivirus packaging; the cell factory adopts a ten-layer cell factory.

进一步的方案是,所述步骤S2中,弃掉细胞工厂中的完全培养基,是将细胞工厂中的完全培养基完全去掉。步骤S2中加入无血清培养基,其目的是把FBS对四质粒的干扰降低到最小。A further solution is that, in the step S2, discarding the complete medium in the cell factory is to completely remove the complete medium in the cell factory. The purpose of adding serum-free medium in step S2 is to minimize the interference of FBS on the four plasmids.

进一步的方案是,所述步骤S3中,转染293T细胞使用PEIpro法,且PEI:DNA(四质粒总数中的DNA数量)按2:1(v/m)进行转染。A further scheme is that in the step S3, PEIpro method is used to transfect 293T cells, and PEI:DNA (the amount of DNA in the total number of four plasmids) is transfected at 2:1 (v/m).

进一步的方案是,所述步骤S3中,十层细胞工厂包装,质粒混合过程中共使用OPTI-MEM 158ml,孵育完成后,需补加至625ml无血清培养基。A further scheme is that in the step S3, ten layers of cell factory packaging are used, and a total of 158 ml of OPTI-MEM is used in the plasmid mixing process. After the incubation is completed, it needs to be supplemented to 625 ml of serum-free medium.

进一步的方案是,所述步骤S4中,转染时间为6小时。In a further scheme, in the step S4, the transfection time is 6 hours.

进一步的方案是,所述步骤S5和S6中,操作的过程中需保持十层细胞工厂平稳,防止培养基强烈晃动使293T细胞漂浮;其中,步骤S5中,加入无血清培养基的量为1250ml。A further scheme is that in the steps S5 and S6, the ten-layer cell factory needs to be kept stable during the operation to prevent the medium from shaking strongly to make the 293T cells float; wherein, in step S5, the amount of serum-free medium added is 1250ml. .

进一步的方案是,所述步骤S7中,Q膜采用的是Mustang Q XT5,离子交换处理中使用的离子交换层析柱的填料为Sepharose 4FF;其中,Q膜富集及离子交换处理采用的纯化仪器为Cytiva的AKTA pure25。A further scheme is that in the step S7, the Q membrane adopts Mustang Q XT5, and the filler of the ion exchange chromatography column used in the ion exchange treatment is Sepharose 4FF; wherein, the Q membrane enrichment and purification adopted in the ion exchange treatment are Sepharose 4FF. The instrument is AKTA pure25 from Cytiva.

进一步的方案是,所述步骤S8中,浓缩后的慢病毒,按体积加入人血白蛋白(HSA)和蔗糖水溶液,混合均匀后,再用0.22滤膜无菌过滤;其中,慢病毒纯化液浓缩的过滤体系液中,人血白蛋白(HSA)和蔗糖的终浓度分别为10%v/v和5%v/v,其目的是确保慢病毒在冻存复苏的过程中保持体内外的渗透压平衡,防止慢病毒损伤。A further scheme is that in the step S8, the concentrated lentivirus is added with human serum albumin (HSA) and sucrose aqueous solution by volume, and after mixing evenly, it is sterile filtered with a 0.22 filter; The final concentrations of human serum albumin (HSA) and sucrose in the concentrated filtration system were 10% v/v and 5% v/v, respectively, to ensure that the lentivirus remained in vitro and in vivo during cryopreservation and resuscitation. Osmolarity balance to prevent lentivirus damage.

进一步的方案是,所述的步骤S8中,慢病毒纯化浓缩过滤后,获得16~25ml左右的慢病毒制剂。In a further scheme, in the step S8, after lentivirus purification, concentration and filtration, a lentivirus preparation of about 16-25 ml is obtained.

进一步的方案是,所述的步骤S9中,慢病毒按实验所需分装,如短期保存可存放于-20℃,长期保存需存放于-80℃。A further scheme is that in the step S9, the lentiviruses are packaged according to the needs of the experiment, and can be stored at -20°C for short-term storage, and at -80°C for long-term storage.

下面通过一些实施例进一步详细说明。The following is further described in detail through some embodiments.

对比例1Comparative Example 1

S01、将处于对数期的8.0×108个293T细胞,含10%FBS完全培养基重悬后转入十层细胞工厂,静置培养;S01. 8.0×10 8 293T cells in logarithmic phase were resuspended in complete medium containing 10% FBS and transferred to a ten-layer cell factory for static culture;

S02、静置培养24h后,弃掉完全培养基,加入625ml无血清培养基,孵育1h;S02. After standing for 24 hours, discard the complete medium, add 625ml of serum-free medium, and incubate for 1 hour;

S03、将四质粒、PEI和OPTI-MEM按比例混合均匀,孵育20min后补无血清培养基至625ml,得到质粒转染混合液;其中,PEI与四质粒总数按2:1(v/m);S03. Mix the four plasmids, PEI and OPTI-MEM evenly in proportion, incubate for 20 min, and then add serum-free medium to 625 ml to obtain a plasmid transfection mixture; among them, the total number of PEI and four plasmids is 2:1 (v/m) ;

S04、将步骤S02中的十层细胞工厂孵育完成后弃掉无血清培养基,加入步骤S03中的质粒转染混合液,转染处理6小时;S04, discard the serum-free medium after the incubation of the ten-layer cell factory in step S02 is completed, add the plasmid transfection mixture in step S03, and conduct the transfection for 6 hours;

S05、转染处理结束后,弃掉质粒转染混合液,加入1250ml完全培养基;S05. After the transfection treatment, discard the plasmid transfection mixture and add 1250ml of complete medium;

S06、分别在第24h和第48h收集慢病毒上清;S06, collect lentiviral supernatant at 24h and 48h respectively;

S07、对收集的慢病毒上清依次进行Q膜富集、核酸酶酶解、离子交换处理,获得慢病毒纯化液;其中,Q膜采用的是Mustang Q XT5,离子交换处理中使用的离子交换层析柱的填料为Sepharose 4FF;其中,Q膜富集及离子交换处理采用的纯化仪器为AKTA pure25;S07. Perform Q membrane enrichment, nuclease enzymatic hydrolysis, and ion exchange treatment on the collected lentivirus supernatant in turn to obtain a lentivirus purified solution; wherein, the Q membrane adopts Mustang Q XT5, and the ion exchange used in the ion exchange treatment The packing of the chromatography column is Sepharose 4FF; among them, the purification instrument used for Q membrane enrichment and ion exchange treatment is AKTA pure25;

S08、将慢病毒纯化液进行超滤浓缩、无菌过滤后,得到慢病毒浓缩液;S08, the lentivirus purified solution is subjected to ultrafiltration concentration and sterile filtration to obtain a lentivirus concentrate;

S09、慢病毒浓缩液分装、冻存,即得到纯化的慢病毒制剂。S09, the lentivirus concentrate is subpackaged and frozen to obtain a purified lentivirus preparation.

实施例1Example 1

S11、将处于对数期的5.5×108个293T细胞,含10%FBS完全培养基重悬后转入十层细胞工厂,静置培养;S11. 5.5×10 8 293T cells in log phase were resuspended in complete medium containing 10% FBS and transferred to the ten-layer cell factory for static culture;

S12、静置培养24h后,弃掉完全培养基,加入500ml无血清培养基,孵育1h;S12. After static culture for 24 hours, discard the complete medium, add 500 ml of serum-free medium, and incubate for 1 hour;

S13、将四质粒、PEI和OPTI-MEM按比例混合均匀,孵育10min后补无血清培养基至625ml,得到质粒转染混合液;其中,PEI与四质粒总数按2:1(v/m);S13. Mix the four plasmids, PEI and OPTI-MEM evenly in proportion, incubate for 10 min, and then add serum-free medium to 625 ml to obtain a plasmid transfection mixture; among them, the total number of PEI and four plasmids is 2:1 (v/m) ;

S14、将步骤S12中的十层细胞工厂孵育完成后弃掉无血清培养基,再加入步骤S13中的质粒转染混合液,转染处理5小时;S14. After the ten-layer cell factory incubation in step S12 is completed, the serum-free medium is discarded, and then the plasmid transfection mixture in step S13 is added, and the transfection is processed for 5 hours;

S15、转染处理结束后,弃掉质粒转染混合液,加入1000ml无血清培养基;S15. After the transfection treatment, discard the plasmid transfection mixture and add 1000 ml of serum-free medium;

S16、分别在第24h和第48h收集慢病毒上清;S16, collect lentiviral supernatant at 24h and 48h respectively;

1S7、对收集的慢病毒上清依次进行Q膜富集、核酸酶酶解、离子交换处理,获得慢病毒纯化液;其中,Q膜采用的是Mustang Q XT5,离子交换处理中使用的离子交换层析柱的填料为Sepharose 4FF;其中,Q膜富集及离子交换处理采用的纯化仪器为AKTA pure25;1S7. Perform Q membrane enrichment, nuclease enzymatic hydrolysis, and ion exchange treatment on the collected lentiviral supernatant in sequence to obtain a lentivirus purified solution; wherein, the Q membrane adopts Mustang Q XT5, and the ion exchange used in the ion exchange treatment The packing of the chromatography column is Sepharose 4FF; among them, the purification instrument used for Q membrane enrichment and ion exchange treatment is AKTA pure25;

S18、将慢病毒纯化液进行超滤浓缩、无菌过滤后,得到慢病毒浓缩液;S18, the lentivirus purified solution is subjected to ultrafiltration concentration and sterile filtration to obtain a lentivirus concentrate;

S19、慢病毒浓缩液分装、冻存,即得到纯化的慢病毒制剂。S19, the lentivirus concentrate is divided and frozen to obtain a purified lentivirus preparation.

实施例2Example 2

S21、将处于对数期的8.0×108个293T细胞,含10%FBS完全培养基重悬后转入十层细胞工厂转染处理;S21. 8.0×10 8 293T cells in log phase were resuspended in complete medium containing 10% FBS and transferred to ten-layer cell factory for transfection treatment;

S22、静置培养24h后,弃掉完全培养基,加入625ml无血清培养基,孵育1h;S22. After standing for 24 hours of culture, discard the complete medium, add 625 ml of serum-free medium, and incubate for 1 hour;

S23、将四质粒、PEI和OPTI-MEM按比例混合均匀,孵育30min后补无血清培养基至625ml,得到质粒转染混合液;其中,PEI与四质粒总数按2:1(v/m);S23. Mix the four plasmids, PEI and OPTI-MEM evenly in proportion, incubate for 30 minutes and then supplement the serum-free medium to 625 ml to obtain a plasmid transfection mixture; among them, the total number of PEI and four plasmids is 2:1 (v/m) ;

S24、将步骤S22中十层细胞工厂孵育完成后弃掉无血清培养基,再加入步骤S23中的质粒转染混合液,转染处理6小时;S24, discard the serum-free medium after the incubation of the ten-layer cell factory in step S22 is completed, then add the plasmid transfection mixture in step S23, and perform the transfection for 6 hours;

S25、转染处理结束后,弃掉质粒转染混合液,再加入1400ml无血清培养基;S25. After the transfection treatment, discard the plasmid transfection mixture, and then add 1400 ml of serum-free medium;

S26、分别在第24h和第48h收集慢病毒上清;S26, collect lentiviral supernatant at 24h and 48h respectively;

S27、对收集的慢病毒上清依次进行Q膜富集、核酸酶酶解、离子交换处理,获得慢病毒纯化液;其中,Q膜采用的是Mustang Q XT5,离子交换处理中使用的离子交换层析柱的填料为Sepharose 4FF;其中,Q膜富集及离子交换处理采用的纯化仪器为AKTA pure25;S27. Perform Q membrane enrichment, nuclease enzymatic hydrolysis, and ion exchange treatment on the collected lentivirus supernatant in sequence to obtain a lentivirus purified solution; wherein, the Q membrane adopts Mustang Q XT5, and the ion exchange used in the ion exchange treatment The packing of the chromatography column is Sepharose 4FF; among them, the purification instrument used for Q membrane enrichment and ion exchange treatment is AKTA pure25;

S28、将慢病毒纯化液进行超滤浓缩、无菌过滤后,得到慢病毒浓缩液;S28, the lentivirus purified solution is subjected to ultrafiltration concentration and sterile filtration to obtain a lentivirus concentrate;

S29、慢病毒浓缩液分装、冻存,即得到纯化的慢病毒制剂。S29, the lentivirus concentrate is divided and frozen to obtain a purified lentivirus preparation.

实施例3Example 3

S31、将处于对数期的10.0×108个293T细胞,含10%FBS完全培养基重悬后转入十层细胞工厂转染处理;S31. 10.0×10 8 293T cells in log phase were resuspended in complete medium containing 10% FBS and transferred to ten-layer cell factory for transfection treatment;

S32、静置培养24h后,弃掉完全培养基,加入700ml无血清培养基,孵育1h;S32. After standing for 24 hours of culture, discard the complete medium, add 700 ml of serum-free medium, and incubate for 1 hour;

S33、将四质粒、PEI和OPTI-MEM按比例混合均匀,孵育20min后补无血清培养基至625ml,得到质粒转染混合液;其中,PEI与四质粒总数按2:1(v/m);S33. Mix the four plasmids, PEI and OPTI-MEM evenly in proportion, incubate for 20 min and then supplement the serum-free medium to 625 ml to obtain a plasmid transfection mixture; among which, the total number of PEI and four plasmids is 2:1 (v/m) ;

S34、将步骤S32中的十层细胞工厂孵育完成后弃掉孵育基,再加入步骤S33中的质粒转染混合液,转染处理7小时;S34. After the ten-layer cell factory incubation in step S32 is completed, discard the incubation base, then add the plasmid transfection mixture in step S33, and perform transfection for 7 hours;

S35、转染处理结束后,弃掉质粒转染混合液,加入1250ml无血清培养基;S35. After the transfection treatment, discard the plasmid transfection mixture and add 1250 ml of serum-free medium;

S36、分别在第24h和第48h收集慢病毒上清;S36, collect lentiviral supernatant at 24h and 48h respectively;

S37、对收集的慢病毒上清依次进行Q膜富集、核酸酶酶解、离子交换处理,获得慢病毒纯化液;其中,Q膜采用的是Mustang Q XT5,离子交换处理中使用的离子交换层析柱的填料为Sepharose 4FF;其中,Q膜富集及离子交换处理采用的纯化仪器为AKTA pure25;S37. Perform Q membrane enrichment, nuclease enzymatic hydrolysis, and ion exchange treatment on the collected lentivirus supernatant in sequence to obtain a lentivirus purified solution; wherein, the Q membrane adopts Mustang Q XT5, and the ion exchange used in the ion exchange treatment The packing of the chromatography column is Sepharose 4FF; among them, the purification instrument used for Q membrane enrichment and ion exchange treatment is AKTA pure25;

S38、将慢病毒纯化液进行超滤浓缩、无菌过滤后,得到慢病毒浓缩液;S38, the lentivirus purified solution is subjected to ultrafiltration concentration and sterile filtration to obtain a lentivirus concentrate;

S39、慢病毒浓缩液分装、冻存,即得到纯化的慢病毒制剂。S39, the lentivirus concentrate is divided and frozen to obtain a purified lentivirus preparation.

二、慢病毒检测分析2. Lentivirus detection and analysis

慢病毒检测结构分析如图2、3、4、5及表1所示。The structural analysis of lentivirus detection is shown in Figure 2, 3, 4, 5 and Table 1.

表1 四种包装方法慢病毒的检测结果Table 1 Detection results of lentiviruses by four packaging methods

Figure 279914DEST_PATH_IMAGE001
Figure 279914DEST_PATH_IMAGE001

对比例1中,按照现有的慢病毒包装工艺进行,包装的过程中采用10%FBS的完全培养基,如图2和表1所示,在纯化的过程中,FBS残留成分会影响慢病毒的出峰,以至于慢病毒的纯度不高,残留检测超标;同时,由于采用完全培养基孵育293T细胞,有血清残留,峰图很杂,对纯化干扰大,造成左边峰值曲线不光滑流畅,这些导致总DNA残留达到38960ng/ml(远超标准值100ng/ml)及BSA残留达到46850ng/5.0*107TU LV(远超标准值500ng/5.0*107TULV)。In Comparative Example 1, according to the existing lentivirus packaging process, a complete medium of 10% FBS was used in the packaging process, as shown in Figure 2 and Table 1. During the purification process, the residual components of FBS will affect the lentivirus. At the same time, due to the use of complete medium to incubate 293T cells, there is residual serum, and the peak graph is very mixed, which greatly interferes with purification, resulting in the left peak curve not smooth and smooth. These resulted in a total DNA residue of 38960ng/ml (far exceeding the standard value of 100ng/ml) and BSA residues reaching 46850ng/5.0*10 7 TULV (far exceeding the standard value of 500ng/5.0*10 7 TULV).

实施例1中,采用小于对比例1的 293T细胞数量包装,包装的过程中采用无血培养基,如图3和表1所示,在纯化的过程中,慢病毒的出峰很干净,慢病毒的纯度高,残留检测达标,但是慢病毒的滴度略低一些;同时,由于采用去血清培养基孵育293T细胞,无血清残留,对纯化干扰小,使的左边峰值曲线光滑流畅,总DNA残留达到29.8ng/ml(低于标准值100ng/ml)及BSA残留为100ng/5.0*107TU LV(低于标准值500ng/5.0*107TU LV)。In Example 1, the number of 293T cells less than that of Comparative Example 1 was used for packaging, and blood-free medium was used in the packaging process. As shown in Figure 3 and Table 1, during the purification process, the lentivirus was very clean and slow. The purity of the virus is high, and the residual detection is up to the standard, but the titer of the lentivirus is slightly lower; at the same time, since the 293T cells are incubated with serum-free medium, there is no serum residue, which has little interference with purification, making the left peak curve smooth and smooth, and the total DNA The residue reached 29.8ng/ml (100ng/ml lower than the standard value) and the BSA residue was 100ng/5.0*10 7 TU LV (500ng/5.0*10 7 TU LV lower than the standard value).

实施例2中,包装工艺中,采用与对比例1一致293T细胞数量,包装的过程中采用无血培养基,如图4和表1所示,在纯化的过程中,慢病毒的出峰干净,慢病毒的纯度高,残留检测达标,慢病毒的滴度比实例2要高很多;同时,由于采用去血清培养基孵育293T细胞,无血清残留,对纯化干扰小,使的左边峰值曲线光滑流畅,总DNA残留达到50.9ng/ml(低于标准值100ng/ml)及BSA残留为98.6ng/5.0*107TU LV(低于标准值500ng/5.0*107TU LV)。In Example 2, in the packaging process, the same number of 293T cells as in Comparative Example 1 was used, and blood-free medium was used in the packaging process, as shown in Figure 4 and Table 1, in the process of purification, the peak of lentivirus was clean. , the purity of the lentivirus is high, and the residual detection is up to the standard, and the titer of the lentivirus is much higher than that of Example 2; at the same time, since the 293T cells are incubated with serum-free medium, there is no serum residue, which has little interference with purification, making the left peak curve smooth. Fluency, the total DNA residue reached 50.9ng/ml (lower than the standard value of 100ng/ml) and the BSA residue was 98.6ng/5.0*10 7 TU LV (lower than the standard value of 500ng/5.0*10 7 TU LV).

实施例3中,与对比例1相比,包装工艺将慢病毒包装293T细胞数量提高,包装的过程中采用无血培养基,如图5和表1所示,在纯化的过程中,慢病毒的出峰带有杂峰,慢病毒的纯度降低,残留检测中总DNA超标,慢病毒的滴度降低;同时, 293T细胞量增大,又由于无血清,细胞存在快速凋亡,此时细胞中的DNA会释放出来,检测时,DNA会超标,总DNA残留达到348ng/ml(高于标准值100ng/ml)及BSA残留为125.9ng/5.0*107TU LV(低于标准值500ng/5.0*107TU LV)。In Example 3, compared with Comparative Example 1, the packaging process increased the number of lentivirus packaging 293T cells, and blood-free medium was used in the packaging process, as shown in Figure 5 and Table 1, during the purification process, the lentivirus The peak of 293T has spurious peaks, the purity of lentivirus decreases, the total DNA in residual detection exceeds the standard, and the titer of lentivirus decreases; at the same time, the amount of 293T cells increases, and due to the absence of serum, the cells have rapid apoptosis, at this time the cells The DNA in the tester will be released. During detection, the DNA will exceed the standard, and the total DNA residue will reach 348ng/ml (100ng/ml higher than the standard value) and the BSA residue will be 125.9ng/5.0*10 7 TU LV (500ng/ml lower than the standard value). 5.0* 107TULV ).

因此,由本发明方案可知:Therefore, it can be known from the scheme of the present invention that:

1、上述对比例1、实施例1-3中,通过比较发现,FBS可以提高慢病毒的滴度,但是对下游纯化的要求更高;细胞的数量及细胞的状态对慢病毒的滴度也有一定的影响;1. In the above comparative example 1 and examples 1-3, it is found by comparison that FBS can increase the titer of lentivirus, but it has higher requirements for downstream purification; the number of cells and the state of cells also affect the titer of lentivirus. certain influence;

2、慢病毒包装的过程中加入FBS,纯化时的峰形不对称,加大了纯化的难度;未加入FBS的实施方案中,包装293T 细胞数量低时,细胞的状态很好,纯化的峰形非常干净,随着包装293T细胞数量的增加,纯化时的峰形中会出现杂峰,所以8.0×108的293T细胞数量为最佳的十层细胞工厂包装数量;2. FBS is added during lentivirus packaging, and the peak shape during purification is asymmetric, which increases the difficulty of purification; in the embodiment without FBS, when the number of packaging 293T cells is low, the state of the cells is very good, and the purified peak The shape of 293T cells is very clean. As the number of packaging 293T cells increases, there will be spurious peaks in the peak shape during purification, so the number of 293T cells of 8.0×10 8 is the optimal ten-layer cell factory packaging number;

3、如图6所示,对比例1中,纯化过程加入含FBS的完全培养基,可以获得最高的慢病毒滴度;实施例1-3中,纯化过程未加入FBS的无血清培养基,慢病毒的滴度会随着包装细胞293T的数量先上升,然后出现下降;3. As shown in Figure 6, in Comparative Example 1, the complete medium containing FBS was added in the purification process to obtain the highest lentivirus titer; in Examples 1-3, the serum-free medium without FBS was added in the purification process, The titer of lentivirus will first increase and then decrease with the number of packaging cells 293T;

4、如表1所示,加入FBS的实施例获得的慢病毒,其BSA超标,同时由于FBS的影响,其总DNA也超标,即,由于加入FBS后,增加了其它残留分离纯化;而未加入FBS的实施例中,293T细胞的数量低的时候更项指标最好,而随着细胞数量的增加,293T的状态变差,以至于实施例3的总DNA残留超标;所以选择8.0×108的293T细胞数量为最佳的十层细胞工厂包装数量。4. As shown in Table 1, the BSA of the lentivirus obtained in the example of adding FBS exceeds the standard, and at the same time, due to the influence of FBS, its total DNA also exceeds the standard, that is, due to the addition of FBS, other residual separation and purification are added; In the example of adding FBS, when the number of 293T cells is low, the index is the best, and as the number of cells increases, the state of 293T becomes worse, so that the total DNA residue in Example 3 exceeds the standard; therefore, 8.0 × 10 was selected. The number of 293T cells of 8 is the optimal ten-layer cell factory packaging number.

总之,在慢病毒细胞293T包装转染结束后,293T细胞纯化中采用无血清培养基孵育,相对于对比例1中完全培养基(含FBS)培养而言,DNA残留和BSA残留都少,且FBS对293T细胞纯化峰图的影响小,有利于获得符合GMP标准的慢病毒。In conclusion, after the packaging and transfection of lentiviral cells 293T, 293T cells were purified by using serum-free medium for incubation. Compared with the complete medium (containing FBS) culture in Comparative Example 1, there were less DNA residues and BSA residues, and FBS has little effect on the purified peaks of 293T cells, which is beneficial to obtain lentiviruses that meet GMP standards.

应当理解的是,上述针对本发明较佳实施例的表述较为详细,并不能因此而认为是对本发明专利保护范围的限制,本发明的专利保护范围应以所附权利要求为准。It should be understood that the above description of the preferred embodiments of the present invention is relatively detailed, and therefore should not be considered as a limitation on the scope of the patent protection of the present invention, and the patent protection scope of the present invention should be subject to the appended claims.

Claims (10)

1.一种慢病毒包装与纯化方法,其特征在于,包括如下步骤:1. a lentivirus packaging and purification method, is characterized in that, comprises the steps: 将处于对数生长期的293T细胞采用完全培养基重悬后转入细胞工厂,静置培养;The 293T cells in logarithmic growth phase were resuspended in complete medium and transferred to the cell factory for static culture; 静置培养24小时后,去掉所述完全培养基,加入无血清培养基,继续孵育;After 24 hours of static culture, remove the complete medium, add serum-free medium, and continue to incubate; 将四质粒、PEI和OPTI-MEM混合均匀后进行孵育,随后补充加入无血清培养基,得到质粒转染混合液;The four plasmids, PEI and OPTI-MEM were mixed evenly and incubated, and then supplemented with serum-free medium to obtain a plasmid transfection mixture; 所述细胞工厂孵育293T细胞完成后去掉无血清培养基,接着往所述细胞工厂加入所述质粒转染混合液,进行转染处理;After incubating the 293T cells in the cell factory, remove the serum-free medium, and then add the plasmid transfection mixture to the cell factory for transfection treatment; 转染处理结束后,去掉所述质粒转染混合液,并加入全新的无血清培养基,静置培养;静置培养过程中,收集慢病毒上清液;After the transfection treatment, the plasmid transfection mixture was removed, and a new serum-free medium was added for static culture; during the static culture, the lentivirus supernatant was collected; 对慢病毒上清液依次进行Q膜富集、核酸酶酶解、离子交换处理后,获得慢病毒纯化液;The lentivirus supernatant was sequentially subjected to Q membrane enrichment, nuclease enzymatic hydrolysis, and ion exchange treatment to obtain a lentivirus purified solution; 所述慢病毒纯化液依次进行超滤浓缩、无菌过滤处理后,获得纯化的慢病浓缩液,然后分装、冻存、备用。After the lentivirus purified solution is subjected to ultrafiltration concentration and sterile filtration treatment in sequence, a purified chronic disease concentration solution is obtained, which is then packaged, frozen, and used for later use. 2.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述293T细胞转入细胞工厂时:293T细胞的转入量为5.0×108~10.0×108;所述细胞工厂为十层细胞工厂;且所述完全培养基为含10%(v/v)FBS的完全培养基。2. The lentivirus packaging and purification method according to claim 1, wherein when the 293T cells are transferred into a cell factory: the transferred amount of the 293T cells is 5.0×10 8 to 10.0×10 8 ; The factory was a ten-layer cell factory; and the complete medium was complete medium with 10% (v/v) FBS. 3.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述293T细胞静置培养24小时后,所述无血清培养基的加入量为500~700ml,且孵育时间为1小时。3. The lentivirus packaging and purification method according to claim 1, characterized in that, after the 293T cells are statically cultured for 24 hours, the added amount of the serum-free medium is 500-700 ml, and the incubation time is 1 Hour. 4.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述质粒转染混合液制备步骤中, PEI与四质粒总数按2:1(v/m);所述孵育时间为10~30分钟。4 . The lentivirus packaging and purification method according to claim 1 , wherein, in the preparation step of the plasmid transfection mixture, the total number of PEI and four plasmids is 2:1 (v/m); the incubation time 10 to 30 minutes. 5.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,质粒混合过程中共使用OPTI-MEM 158ml,孵育完成后,需补加至625ml无血清培养基。5 . The lentivirus packaging and purification method according to claim 1 , wherein 158 ml of OPTI-MEM is used in the plasmid mixing process, and after incubation, it needs to be supplemented to 625 ml of serum-free medium. 6 . 6.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述质粒转染处理步骤中,转染处理时间为5~7小时。6 . The lentivirus packaging and purification method according to claim 1 , wherein, in the plasmid transfection treatment step, the transfection treatment time is 5-7 hours. 7 . 7.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述质粒转染处理结束后,加入全新的所述无血清培养基的量为1000~1400ml。7 . The lentivirus packaging and purification method according to claim 1 , wherein, after the plasmid transfection treatment is completed, the amount of the new serum-free medium added is 1000-1400 ml. 8 . 8.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述慢病毒上清液的收集时间分别是在静置培养的第24小时和第48小时。8 . The lentivirus packaging and purification method according to claim 1 , wherein the collection time of the lentivirus supernatant is the 24th hour and the 48th hour of static culture, respectively. 9 . 9.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述慢病毒上清液处理步骤中,所述Q膜采用的是Mustang Q XT5;离子交换处理中使用的离子交换层析柱的填料为Sepharose 4FF。9. The lentivirus packaging and purification method according to claim 1, wherein in the lentivirus supernatant treatment step, the Q membrane adopts Mustang Q XT5; the ion exchange used in the ion exchange treatment The packing of the chromatography column is Sepharose 4FF. 10.根据权利要求1所述的慢病毒包装与纯化方法,其特征在于,所述慢病毒纯化液浓缩的过滤处理还包括:浓缩后的慢病毒,加入终浓度为10%v/v的人血白蛋白和终浓度为5(v/v)的蔗糖水溶液,混合均匀后,再用0.22滤膜无菌过滤。10. The lentivirus packaging and purification method according to claim 1, wherein the concentrated filtration treatment of the lentivirus purified solution further comprises: adding the concentrated lentivirus with a final concentration of 10% v/v human Serum albumin and sucrose aqueous solution with a final concentration of 5 (v/v) were mixed uniformly, and then sterile filtered through a 0.22 filter membrane.
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