昆虫杆状病毒表达载体系统与疫苗研制的30年回顾

1983年12月,一篇关于用昆虫杆状病毒感染昆虫细胞表达重组人β干扰素文章的发表,标示了杆状病毒表达载体系统(Baculovirus expression vector system,BEVS)的诞生。迄今为止,已采用BEVS表达生产了数千种重组蛋白,其中7种已被成功用于商品化人用或兽用疫苗的抗原。仅对30年来基于BEVS的疫苗研制作一论述。     

昆虫杆状病毒表达系统的研究与应用进展

昆虫杆状病毒表达系统 (BEVS)因具有完备的翻译后加工修饰系统和高效表达外源基因的能力等特点 ,现已成功表达了近千种高价值蛋白。随着杆状病毒载体的不断改进 ,该系统获得重组病毒的几率已从最初的 0 1 %～ 1 %提高到现在的 80 %～ 90 %以上 ,并且出现了一些新的宿主域扩大的昆虫杆状病毒载体和高水平表达重组蛋白的昆虫细胞系。杆状病毒载体将在未来药物研发、疫苗生产、基因治疗、重组杆状病毒杀虫剂等领域得到广泛应用。但存在的一些问题如杆状病毒的基因组学研究相对薄弱 ,有关病毒晚期基因的高表达和调控机制等还不十分清楚 ,表达产物的纯化比较困难 ,多元表达等方面的技术还不够成熟等 ,均有待进一步解决。     

杆状病毒基因工程进展

近年来,应用昆虫杆状病毒作载体在昆虫细胞或虫体中高效表达外源基因的技术已得到广泛的推广应用。这一基因工程系统安全、高效、容量大,表达产物具有生物活性,是很有潜力的系统之一,已有数百种动物、植物、微生物,病毒的基因在这一系统中成功表达,并有多篇综述文章和专著详细介绍这一载体表达系统。本文将概述杆状病毒分子生物学及基因工程的基本原理,主要介绍近几年来的研究与进展。     

昆虫杆状病毒应用于哺乳动物基因治疗的研究进展

杆状病毒是一类宿主特异性的昆虫病毒。昆虫杆状病毒表达系统是一个高效的真核表达系统,被广泛用于在昆虫细胞或昆虫幼虫中生产外源蛋白质。杆状病毒不能感染哺乳动物,却可以进入不同物种和组织来源的多种哺乳动物细胞,并在合适的哺乳动物启动子控制下表达外源基因。杆状病毒在哺乳动物细胞中不能复制,对细胞没有毒性,加上杆状病毒本身具有基因组大、可操作性好等优点,作为哺乳动物基因治疗的载体,将治疗基因传递给哺乳动物细胞已受到了广泛关注。在此就杆状病毒作为基因治疗载体的最新研究进展进行了阐述并探讨其发展趋势。     

重组杆状病毒：一种新型哺乳动物细胞基因转移载体

昆虫杆状病毒表达载体系统已广泛应用于表达重组蛋白。近年来研究显示,含有哺乳动物细胞启动子元件的重组杆状病毒可有效地转导多种哺乳动物原代和传代细胞。借助于杆状病毒载体,已成功实现了外源基因在哺乳动物细胞内的瞬时或稳定表达;而在体内,杆状病毒可被血清中的补体成份所灭活,从而抑制了转导效率,但是通过对杆状病毒进行修饰（如伪型杆状病毒）,可以抵抗补体的灭活作用。研究人员对杆状病毒转导机制进行了探索,但是至今尚未完全弄清。杆状病毒基因转移系统最大特点是,杆状病毒能在昆虫细胞内大量繁殖,而不能在哺乳动物细胞内复制,因而具有很高的生物安全性;同时,此系统还具有操作简便、插入外源基因容量大等优点,使得杆状病毒作为哺乳动物细胞的基因传递载体,具有广泛的应用前景。     

昆虫杆状病毒表达系统的研究进展与应用

昆虫杆状病毒表达载体系统具有安全性好、重组蛋白表达量高、能同时表达多个基因、重组蛋白翻译后加工完整等特点,因而得到了广泛的应用。随着重组杆状病毒构建技术的不断发展,昆虫杆状病毒表达载体系统的操作在逐渐简化,重组杆状病毒获得的效率也在不断提高。昆虫细胞培养技术的改进和转基因昆虫细胞系的发展,进一步推动了昆虫杆状病毒表达载体系统在商品化药物、治疗性抗体、生物农药研发和基因治疗中的应用。尽管仍存在着重组蛋白降解的问题,但随着分子生物学技术的发展,对杆状病毒载体的研究与改造也会更加深入,未来昆虫杆状病毒表达载体系统的应用将更为广泛。     

牛γ-干扰素在重组杆状病毒中的表达及其抗病毒活性的测定

研究利用Bac-To-Bac杆状病毒表达系统构建含有牛γ-干扰素(Bovine interferon-γ,BoIFN-γ)完整开放阅读框的供体质粒pFastBacTM1-BoIFN-γ,转化DH10Bac感受态细胞获得重组穿梭质粒rBacmid-BoIFN-γ,转染sf9昆虫细胞救获表达BoIFN-γ的重组杆状病毒rBac-BoIFN-γ。采用抗BoIFN-γ单克隆抗体作为一抗进行间接免疫荧光(IFA)及间接ELISA检测,表明BoIFN-γ在重组杆状病毒rBac-BoIFN-γ感染的sf9昆虫细胞中获得正确表达。利用VSV*GFP-MDBK细胞系统测定rBoIFN-γ抗病毒活性,重组杆状病毒表达重组BoIFN-γ(rBoIFN-γ)能有效抑制水疱性口炎病毒(VSV)在牛肾细胞(MDBK)上的复制,rBac-BoIFN-γ感染sf9昆虫细胞上清抗病毒活性为2×105IU/mL,而且其抗病毒活性可以被鼠抗原核表达重组BoIFN-γ免疫血清阻断。结果表明:rBoIFN-γ在重组杆状病毒rBac-BoIFN-γ感染的sf9昆虫细胞中获得良好表达,并具有高效抗病毒活性。     

杆状病毒-昆虫细胞表达系统在复合体重组表达应用中的研究进展

真核细胞大部分生命活动是通过复合体催化的。因此,系统了解这些复合体的生物学功能,将在健康和疾病方面具有重要意义。由于内源性复合体存在低丰度和异质性特点,因而直接提取复合体存在一定的困难。杆状病毒-昆虫细胞表达系统可成功表达复合体,为研究复合体的结构和功能提供新的手段。综述近年来利用杆状病毒-昆虫细胞表达系统进行蛋白质复合体结构和功能研究的进展。     

猪γ-干扰素在重组杆状病毒中的表达及其抗病毒活性的测定

研究利用Bac-To-Bac杆状病毒表达系统构建含有猪γ-干扰素(porcine interferon-γ,PoIFN-γ)完整开放阅读框的供体质粒pFastBacTM1-PoIFN-γ,转化DH10Bac感受态细胞获得重组穿梭质粒rBacmid-PoIFN-γ,转染sf9昆虫细胞救获表达PoIFN-γ的重组杆状病毒rBac-PoIFN-γ。以抗PoIFN-γ单克隆抗体为一抗进行Western blot、间接免疫荧光(IFA)及间接ELISA检测,结果表明PoIFN-γ在重组杆状病毒rBac-PoIFN-γ感染的昆虫细胞中获得正确表达。抗病毒活性试验显示,重组杆状病毒表达rPoIFN-γ能有效抑制水疱性口炎病毒(VSV)在猪肾细胞系(PK-15)的复制,rBac-PoIFN-γ感染昆虫细胞培养上清抗病毒活性为2×104抑制单位(IU)/mL,其抗病毒活性可以被鼠抗原核表达重组PoIFN-γ免疫血清有效阻断。结果表明rPoIFN-γ在重组杆状病毒rBac-PoIFN-γ在感染昆虫细胞获得有效表达,并具有高效抗病毒活性。     

杆状病毒载体及其在昆虫细胞中表达外源基因的研究进展

本文介绍了杆状病毒载体在昆虫细胞中表达外源基因的基本策略和发展趋势。杆状病毒载体系统近年来已被人们广泛用来表达人类、动物和植物等的一些重要蛋白质分子,在医学、农业等领域的基因工程研究中发挥了越来越大的作用。杆状病毒载体系统表达外源基因的效率高,表达产物的结构和活性与天然产物一致,为当今基因工程研究中最有发展前途的病毒载体表达系统。     

表达抗-CD25单克隆抗体的GS-NS0骨髓瘤细胞无血清培养及代谢特性

抗-CD25单克隆抗体作为免疫抑制剂拥有广阔的市场前景和巨大的经济价值。本实验以表达抗?CD25单克隆抗体的GS-NS0细胞为研究对象,开发了支持其大规模培养和抗体表达的无血清低蛋白培养基,批培养最大活细胞密度和最大抗体浓度分别达3×106cells/mL和300mg/L以上,比商业无血清培养基(Excell 620+0.2% primatone)分别提高了100%和46%。通过批培养实验,研究了细胞的生长、葡萄糖和氨基酸代谢、以及产物表达特点,并揭示了批培养过程中初始葡萄糖浓度对GS-NS0细胞生长与代谢的影响规律。为优化GS-NS0细胞培养过程和抗CD25单抗成功迈向产业化提供了重要的科学依据。     

Effects of cell density and glucose and glutamine levels on the respiration rates of hybridoma cells

The effects of cell density as well as the concentration levels of glucose and glutamine on the specific respiration rate of a hybridoma cell line were investigated. The experimental oxygen consumption rate was found to be constant over a wide range of dissolved oxygen levels if the suspension medium contained glutamine. In glutamine-free medium, however, the rate of oxygen consumption decreased slowly with time.In a stationary flask batch culture, the specific respiration rate decreased from about 7 to 2.9 mumol/min per 10(9) cells as the cell density increased exponentially from 1 x 10(5) to 1.2 x 10(6)/mL. To isolate the effect of cell density, cells were re suspended in fresh culture medium so that nutrient concentrations were the same for all experiments. The specific respiration rate decreased with increasing cell density in the same manner as in the stationary flask culture, falling from 8 to 4 mumol/min per 10(9) cells as the cell density increased from 10(5) to 10(6) cells/mL, then declining to 2 mumol/min per 10(9) cells when the cell density reached 10(7) cells/mL.Cells suspended in Hanks balanced sale solution (HBSS) were used to elucidate the effect of glucose and glutamine levels on respiration. The addition of glucose in concentrations of 0.25, 0.50, and 0.75 g/L had no observable effect on the specific oxygen uptake rate; however, a glucose concentration of 1 g/L reduced the uptake rate by 22%. Glutamine in a concentration of 0.30 g/L increased the specific respiration rate in HBSS containing 0 and 1 g/L glucose by approximately 13%.     

Growth kinetics of Chinese hamster ovary cells in a compact loop bioreactor. 3. Selection and characterization of an anchorage-independent subline and medium improvement.

Four sublines of Chinese hamster ovary (CHO) cells were selected or cloned on a 10% fetal calf serum supplemented MEM-alpha medium. Three of them were monolayer cultures and could proliferate by 2000 times a week (mu = 1.1 d 1) in T-flasks. The other subline, S1, could grow in suspension even in static T-flask cultures. The stability in chromosome number of these cell lines was investigated. By evaluating the kinetic growth parameters, i.e. the specific rates of growth, glucose consumption and lactic acid production, and the yields of cells and lactic acid from glucose, the S1 cells were considered to be the most suitable subline for the bioreactor suspension culture. The S1 cells reached the greatest maximum of cell concentration among all cell lines tested because of their efficient glucose utilization. Observed nutrient limitations in the S1 cell culture was overcome by modification of the medium composition, that is addition of 10 mg l-1 hypoxanthine, 1 mg l-1 FeSO4.7H2O, and 0.1 mg l-1 sodium putrescine, elimination of glutamine, supplementation of 6 mM asparagine and double amount of isoleucine, leucine, methionine and vitamins other than ascorbic acid, cyanocobalamin and biotin, increase of NaHCO3 concentration from 26 to 40 mM, and finally decrease of NaCl concentration from 122 to 100 mM. With this modified medium, 7.2 X 10(6) ml-1 of the maximum cell concentration was observed in a glucose fed-batch culture, the cell concentration which was twice as much as in batch cultures with the original medium.     

Requirement of heme for growth of Bacteroides fragilis.

Heme or protoporphyrin IX was required for growth of Bacteroides fragilis in a defined medium. The amount of heme necessary for half-maximal growth was 2 to 10 ng/ml (3.8 to 15 pmol/ml) among the Bacteroides species and strains tested. The growth rate, metabolic products from glucose fermentation, and cell yields were affected by the concentration of heme in the medium and by the length of time the culture was incubated. When heme was growth limiting (4 ng/ml), growth rates decreased by 50%, cultures started producing lactic and fumaric acids, and the cell yields declined. The cell yield for B. fragilis (ATCC 25285) at 24 h in medium containing 6.5 microgram of heme per ml was 69 g (dry weight) of cells per mol of glucose compared to 16 g (dry weight) of cells per mol of glucose with 4 ng of heme per ml. B. fragilis was unable to grow in defined medium when a porphyrin precursor, delta-aminolevulenic acid or porphobilinogen, was added in place of heme.     

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 …

基于ｒ２１昆虫细胞在浮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,Ｓ１ｆ２１细胞在两种具代表性的昆虫水解物）的间歇补加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部都到有效的延长。ＴＣ     

Kinetic study on pH dependence of growth and death of Streptococcus faecalis

A chemostat culture was used for lactic acid fermentation with Streptococcus faecalis at various pH values (8.0, 7.0, 6.0, 5.5, 5.0) and glucose concentrations (10, 20, 30 g/l). At every pH value, the reciprocals of the specific consumption rate of glucose and the specific production rate of lactic acid were linearly correlated to the reciprocal of the specific growth rate. The product, lactic acid, caused non-competitive inhibition of the specific growth rate at every pH value. Moreover, it was found that the cell death rate was dependent on pH and lactic acid. The death rate was smallest at pH 7.0 and increased with increasing lactic acid concentration. The kinetic equations of growth and death are proposed in a broader pH range. Correspondence to: H. Ohara     

Improvement of recombinant protein production with the human adenovirus/293S expression system using fed-batch strategies

The human adenovirus/293S cell expression system is used for the production of either recombinant protein or adenovirus vectors for use in gene therapy. In this work, the production of protein tyrosine phosphatase (PTP1C) was used as a model for the scale-up of both applications. Maximum specific production of 30 to 45 mug of active protein/10(6) cells was maintained upon infection with adenovirus vectors at cell densities between 2 x 10(6) to 3 x 10(6) cells/mL in a 3.5-L bioreactor. This was achieved by resuspending the culture in fresh medium at infection time. The pH was kept at 7.0 throughout the experiment and, at 24 h postinfection, glucose and essential amino acids were added. Attempts to replace the complete change of medium at the time of infection with nutrient supplementation of the used medium led to lower production levels, suggesting that protein expression was limited not by the absence of a key nutrient but by inhibitory factors. Two potentially inhibitory factors were investigated: lactic acid accumulation and increased osmolarity. Medium acidification such as that which would be brought about by lactic acid accumulation was shown to depress PTP1C production. The lactate molecule itself decreased the cell viability when added in concentrations of 20 mM or more. But the specific productivity was affected at higher lactate concentrations of 40 mM or more. Additions of glucose, amino acids, and NaHCO(3) used to control pH, led to increases in osmolarity. Osmolarities above 400 mOsm lowered cell density. However, specific production was not significantly affected below 500 mOsm. But, at 500 mOsm, PTP1C production peak was shifted from 48 to 72 hpi. Because of the cell loss, this per cell yield increase did not translate into higher volumetric production. When glucose concentrations was kept at 5 mM by fed-batch addition, lactate production and increases in osmolarity were reduced. In shake flasks, this method permitted maximum production with cells resuspended either in fresh or spent medium at infection. This fed-batch process was implemented successfully at the 3.5-L scale. Fed-batch with glucose may provide a means to increase infected-cell density beyond 3 x 10(6) cells/mL.     

Optimization of virus yield as a strategy to improve rabies vaccine production by Vero cells in a bioreactor

To improve rabies vaccine production by Vero cells, we have developed a strategy based on high cell density culture and optimization of virus yield. We have first optimized cell growth in spinner flask using a Taguchi's L8 experimental design. We analyzed the effects of the following factors: initial glucose and glutamine concentrations, Cytodex 1 concentration and the regulation of glucose level at 1 g l(-1). We have also investigated the effect of the following factor interactions: Cytodex 1 concentration/glutamine concentration, Cytodex 1 concentration/glucose concentration and glucose concentration/glutamine concentration. Statistical analysis of the collected data pointed to the initial glucose concentration, the regulation of glucose level at 1 g l(-1) and the interactions between Cytodex 1 concentration/initial glucose concentration and Cytodex 1 concentration/initial glutamine concentration as the parameters that affected cell growth. Using the optimal conditions determined earlier, we have studied Vero cell growth in a 7-l bioreactor and in batch culture, and obtained a cell density level equal to 3.6 +/- 0.2 x 10(6) cells ml-1. Cell infection with rabies virus (LP 2061/Vero strain) at a multiplicity of infection (MOI) of 0.3 using M199 medium supplemented with 0.2% bovine serum albumin (BSA), yielded a maximal virus titer equal to 8 +/- 1.6 x 10(7) Fluorescent Focus Units (FFU) ml-1. We have also studied Vero cell growth in a 7-l bioreactor using recirculation as a perfusion culture mode during cell proliferation step and perfusion for virus multiplication phase. In comparison to batch culture, we reached a higher cell density level that was equal to 10.1 +/- 0.5 x 10(6) cells ml-1. Cell infection under the conditions previously indicated, yielded 14l of virus harvest that had a virus titer equal to 2.6 +/- 0.5 x 10(7) FFU ml-1. The activity of the inactivated virus harvest showed a protective activity that meets WHO requirements.     

Reduction of waste product excretion via nutrient control: Possible strategies for maximizing product and cell yields on serum in cultures of mammalian cells

Mammalian cells grown in culture excrete lactic acid and ammonium ions in quantities that may limit growth and reduce product synthesis. Frequent replenishment of the culture medium is often necessary to prevent waste product accumulation which could inhibit cell growth. Since increased medium replenishment results in increased usage of animal serum, the most expensive raw material, excessive production of waste products lowers the cell and product yield on serum, and hence increases production costs. Strategies for reducing the production of lactic acid and ammonium bymammalian cells via controlled addition of glucose and glutamine will be demonstrated. Mathematical relations coupling ammonium and glutamine kinetics will be described. Additionally, a method for automatic on-line estimation of the cell concentration was developed. This method involves calculating the ATP production rate from the oxygen uptake rate and the lactic acid production rate. Automatic online estimation of the cell concentration is critical if nutrient levels in large-scale mammaliancell cultures are to be accurately maintained via process control.     

Batch propagation of Lactobacillus helveticus for production of lactic acid from lactose concentrated cheese whey with microaeration and nutrient supplementation

Continuous mix batch bioreactors were used to study the kinetic parameters of lactic acid fermentation in microaerated-nutrient supplemented, lactose concentrated cheese whey using Lactobacillus helveticus. Four initial lactose concentrations ranging from 50 to 150 g l^–1 were first used with no microaeration and no yeast extract added to establish the substrate concentration above which inhibition will occur and then the effects of microaeration and yeast extract on the process kinetic parameters were investigated. The experiments were conducted under controlled pH (5.5) and temperature (42 °C) conditions. The results indicated that higher concentrations of lactose had an inhibitory effect as they increased the lag period and the fermentation time; and decreased the specific growth rate, the maximum cell number, the lactose utilization rate, and the lactic acid production rate. The maximum lactic acid conversion efficiency (75.8%) was achieved with the 75 g l^–1 initial lactose concentration. The optimum lactose concentration for lactic acid production was 75 g l^–1 although Lactobacillus helveticus appeared to tolerate up to 100 g l^–1 lactose concentration. Since the lactic acid productivity is of a minor importance compared to lactic acid concentration when considering the economic feasibility of lactic acid production from cheese whey using Lactobacillus helveticus, a lactose concentration of up to 100 g l^–1 is recommended. Using yeast extract and/or microaeration increased the cell number, specific growth rate, cell yield, lactose consumption, lactic acid utilization rate, lactic acid concentration and lactic acid yield; and reduced the lag period, fermentation time and residual lactose. Combined yeast extract and microaeration produced better results than each one alone. From the results it appears that the energy uncoupling of anabolism and catabolism is the major bottleneck of the process. Besides lactic acid production, lactose may also be hydrolysed into glucose and galactose. The -galactosidase activity in the medium is caused by cell lysis during the exponential growth phase. The metabolic activities of Lactobacillus helveticus in the presence of these three sugars need further investigation.