Stringent regulation and high-level expression of heterologous genes in Escherichia coli using T7 system controllable by the araBAD promoter

The recombinant Eschreichia coli strain BL21 (BAD) was constructed to carry a chromosomal copy of T7 gene 1 fused to the araBAD promoter. To further characterize this expression system, strain BL21 (BAD) was transformed with the plasmid containing the carbamoylase gene from Agrobacterium radiobacter driven by the T7 promoter. Upon induction with L-arabinose, recombinant cells produced 100-fold increase in carbamoylase activity in comparison with uninduced cells on M9 semidefined medium plus glycerol. This protein yield accounts for 30% of total cell protein content. In addition, it was found that after 100 generations the plasmid harboring the carbamoylase gene remained firmly stable in strain BL21 (BAD), but its stability dropped to only 20-30% in strain BL21 (DE3), a commercial strain bearing T7 gene 1 regulated by the lacUV5 promoter in its chromosome. In an attempt to enhance the total protein yield, fed-batch fermentation process was carried out using a two-stage feeding strategy to compartmentalize cell growth and protein synthesis. In the batch fermentation stage, the culture was grown on glucose to reach the stationary growth phase. Subsequently, glycerol was fed to the culture broth and L-arabinose was augmented to induce protein production when cells entered the late log growth phase. As a result, a carbamoylase yield corresponding to 5525 units was obtained, which amounts to a 337-fold increase over that achieved on a shake-flask scale. Taken together, these results illustrate the practical usefulness of T7 system under control of the araBAD promoter for heterologous protein production.     

Fermentation strategies for 1,3-propanediol production from glycerol using a genetically engineered Klebsiella pneumoniae strain to eliminate by-product formation

We generated a genetically engineered Klebsiella pneumoniae strain (AK-VOT) to eliminate by-product formation during production of 1,3-propanediol (1,3-PD) from glycerol. In the present study, the glycerol-metabolizing properties of the recombinant strain were examined during fermentation in a 5 L bioreactor. As expected, by-product formation was completely absent (except for acetate) when the AK-VOT strain fermented glycerol. However, 1,3-PD productivity was severely reduced owing to a delay in cell growth attributable to a low rate of glycerol consumption. This problem was solved by establishing a two-stage process separating cell growth from 1,3-PD production. In addition, nutrient co-supplementation, especially with starch, significantly increased 1,3-PD production from glycerol during fed-batch fermentation by AK-VOT in the absence of by-product formation.     

Engineered transient and stable overexpression of translation factors eIF3i and eIF3c in CHOK1 and HEK293 cells gives enhanced cell growth associated with increased c-Myc expression and increased recombinant protein synthesis

There is a desire to engineer mammalian host cell lines to improve cell growth/biomass accumulation and recombinant biopharmaceutical protein production in industrially relevant cell lines such as the CHOK1 and HEK293 cell lines. The over-expression of individual subunits of the eukaryotic translation factor eIF3 in mammalian cells has previously been shown to result in oncogenic properties being imparted on cells, including increased cell proliferation and growth and enhanced global protein synthesis rates. Here we report on the engineering of CHOK1 and HEK cells to over-express the eIF3i and eIF3c subunits of the eIF3 complex and the resultant impact on cell growth and a reporter of exogenous recombinant protein production. Transient over-expression of eIF3i in HEK293 and CHOK1 cells resulted in a modest increase in total eIF3i amounts (maximum 40% increase above control) and an approximate 10% increase in global protein synthesis rates in CHOK1 cells. Stable over-expression of eIF3i in CHOK1 cells was not achievable, most likely due to the already high levels of eIF3i in CHO cells compared to HEK293 cells, but was achieved in HEK293 cells. HEK293 cells engineered to over-express eIF3i had faster growth that was associated with increased c-Myc expression, achieved higher cell biomass and gave enhanced yields of a reporter of recombinant protein production. Whilst CHOK1 cells could not be engineered to over-express eIF3i directly, they could be engineered to over-express eIF3c, which resulted in a subsequent increase in eIF3i amounts and c-Myc expression. The CHOK1 eIF3c engineered cells grew to higher cell numbers and had enhanced cap- and IRES-dependent recombinant protein synthesis. Collectively these data show that engineering of subunits of the eIF3 complex can enhance cell growth and recombinant protein synthesis in mammalian cells in a cell specific manner that has implications for the engineering or selection of fast growing or high producing cells for production of recombinant proteins.     

Overproduction of alkaline polygalacturonate lyase in recombinant Escherichia coli by a two-stage glycerol feeding approach

This work aims to achieve the overproduction of alkaline polygalacturonate lyase (PGL) with recombinant Escherichia coli by a two-stage glycerol feeding approach. First, the PGL coding gene from Bacillus subtilis WSHB04-02 was expressed in E. coli BL21 (DE3) under the strong inducible T7 promoter of the pET20b (+) vector. And then the influence of media composition, induction temperature, and inducer isopropyl β-D-1-thiogalactopyranoside (IPTG) concentration on cell growth and PGL production was investigated. Finally, a two-stage glycerol feeding strategy was proposed and applied in a 3-L fermenter, where cultivation was conducted at a controlled specific growth rate (μset=0.2) during pre-induction phase, followed by a constant glycerol feeding rate of 12 ml h(-1) at post-induction phase. The total PGL yield reached 371.86 U mL(-1), which is the highest PGL production by recombinant E. coli expression system.     

Improved production of recombinant ovine interferon-tau by mut(+) strain of Pichia pastoris using an optimized methanol feed profile

Recombinant ovine interferon-tau (r-oIFN-tau) production by Pichia pastoris was studied using methanol as the sole carbon source during induction. The cells were grown on glycerol up to a certain cell density before induction of the AOX1 promoter by methanol for expression of the recombinant protein. Cell growth on methanol has been modeled using a substrate-feed equation, which served as the basis for an effective computer control of the process. The r-oIFN-tau concentration in the culture began to decline despite continued cell growth after 50 (+/- 6) h of induction, which was associated with an increase in proteolytic activity of the fermentation broth. A specific growth rate of 0.025 h(-1) was found to be optimal for r-oIFN-tau production. No significant improvement in r-oIFN-tau production was observed when the specific growth rate was stepped up before the critical point when r-oIFN-tau concentration started decreasing during fermentation. However, best results were obtained when the specific growth rate was stepped down from 0.025 to 0.02 h(-1) at 38 h of induction, whereby the active production period was prolonged until 70 h of induction and the broth protease activity was correspondingly reduced. The corresponding maximum protein yield was 391.7 mg x L(-1) after 70 h of fermentation. The proteolytic activity could be reduced by performing fermentations at specific growth rates of 0.025 h(-1) or below. The recombinant protein production can be performed at an optimal yield by directly controlling the methanol feed rate by a computer-controlled model. The production profile of r-oIFN-tau was found to be significantly different from other secreted and intracellular recombinant protein processes, which is an indication that recombinant protein production in Pichia pastoris needs to be optimized as individual processes following established principles.     

Production of hepatitis B surface antigen (preS2 + S) by high-cell density cultivations of a recombinant yeast.

A high-cell density bioprocess has been developed for the production of hepatitis B surface protein (preS2 + S) by recombinant yeast. This fed-batch process utilizes a growth medium containing yeast extract, soy peptone and glucose which was fed at a constant rate to maintain cells in a respiratory state. Cell densities of up to 60 g l-1 dry weight were achieved, which represented a 6-fold increase over those from batch bioprocesses. This increase in cell mass was attained without compromising specific activity; therefore, volumetric productivities of six times those of batch bioprocesses were achieved.     

碳源对重组大肠杆菌发酵生产GLP-1融合蛋白的影响

以一株表达人胰高血糖素样肽-1融合蛋白的重组大肠杆菌为研究对象,首先通过摇瓶实验对碳源种类进行了初步选择,发现葡萄糖和甘油对菌体生长以及GLP-1融合蛋白表达较为适宜。进一步在5 L反应器上对初始葡萄糖及甘油浓度进行了考察,发现高浓度碳源有利于菌体生长却抑制GLP-1融合蛋白表达,但能提高GLP-1融合蛋白的体积得率。在0.25%初始葡萄糖或甘油存在的条件下,在培养过程中流加葡萄糖或甘油维持其在发酵液中的浓度,比较了两者对菌体生长以及GLP-1融合蛋白表达的影响,结果发现,以甘油为碳源时,菌体生长以及GLP-1融合蛋白的表达量均高于以葡萄糖为碳源的结果,最终发酵液的菌浓(OD_(600))可达到25.4,较葡萄糖为碳源时19.1提高了33.0%,GLP-1融合蛋白表达水平和体积得率分别可达到22.4%和1.051 g/L,较葡萄糖为碳源的15.8%和0.504 g/L分别提高41.8%和108.5%。该结果对GLP-1融合蛋白表达菌株发酵条件的进一步优化提供了依据。     

Enhanced production of recombinant rabies virus glycoprotein (rRVGP) by Drosophila melanogaster S2 cells through control of culture conditions

Culture conditions that affect product quality are important to the successful operation and optimization of recombinant protein production. The objective of this study was to optimize culture conditions for growth of recombinant Drosophila melanogaster S2 cells (S2AcRVGP) in order to enhance the production of rRVGP. The addition of DMSO and glycerol to the medium and growth at a reduced temperature (22 °C) were the culture condition variations selected to be tested. Experimental cultures were first performed in serum-free Sf900 II medium in 250 ml Schott flasks. The most promising conditions identified in these experiments were also tested on a higher scale in a 3l bioreactor. In the Schott flasks experiments, all the changes in culture conditions resulted in an increase of rRVGP production. The protein concentration was 3.6-fold higher with addition of 1% DMSO and 1% glycerol and 9.3-fold higher when the cells were cultured at 22 °C instead of the standard 28 °C. The maximum concentration of rRVGP reached was 591 μg l⁻¹. In bioreactor experiments, with control of pH at 6.20 and DO at 50%, the reduced culture temperature (22 °C) was the strategy that promoted the highest glycoprotein production, 928 μg l⁻¹.     

A two-stage cultivation process for the growth enhancement of Chlorella vulgaris

This study proposes a two-stage cultivation process with an autotrophic growth followed by a mixotrophic process. The results indicated that a two-stage cultivation process using a daily dose of 3 g/L of glucose could achieve 7.4 g/L of biomass, which was about a 64 % increase over simple autotrophic cultivation. In the second stage of mixotrophic cultivation, glucose was regarded as a better carbon source for cell growth, than was glycerol. Linoleic acid (C18:2) would be the primary component in the two-stage cultivation as in the autotrophic cultivation. Even carbon source was provided in the second stage of mixotrophic cultivation; lower light intensity limited the mixotrophic growth, which indicated that photosynthesis still plays an important role in the second stage of mixotrophical cultivation. The final biomass was higher after this two-stage cultivation process, which made it suitable for application in the production scale-up of algal biomass.     

Improving performance of mammalian cells in fed-batch processes through "bioreactor evolution"

The amount of recombinant product obtained from mammalian cells grown in a bioreactor is in part limited by achievable cell densities and the ability of cells to remain viable over extended periods of time. In an attempt to generate cell lines capable of better bioreactor performance, we subjected the DG44 Chinese Hamster Ovary (CHO) host cell line and a recombinant production cell line to an iterative process whereby cells capable of surviving the harsh conditions in the bioreactor were selected. This selective process was termed "bioreactor evolution". Following the selective process, the "evolved" host cells attained a 2-fold increase in peak cell density and a 72% increase in integral cell area. Transient transfection experiments demonstrate that the evolved cells have the same transfection efficiency and the same secretory potential as the initial cells. The "evolved" host was also found to contain a large subpopulation of cells that did not require insulin for growth. From this, a new population of growth-factor-independent cells was obtained. These improvements in host properties should prove beneficial in the expression of recombinant proteins in fed-batch processes. The selective process was also applied to a recombinant production cell line. The evolved cells from this selection exhibited a 38% increase in peak cell density, a 30% increase in integral cell area, and a 36% increase in product titer. These increases were obtained without any appreciable impact on product quality, demonstrating the usefulness of this simple approach to improve the performance of recombinant cell lines.     

High cell density culture of Yarrowia lipolytica using a one-step feeding process

Yarrowia lipolytica is a potentially useful host for heterologous protein production. To develop an efficient culture method for high cell density cultivation and heterologous gene expression of Y. lipolytica, the effects of medium components and their concentrations on the growth of Y. lipolytica have been investigated. Addition of yeast extract to the culture media was found to significantly reduce the long lag phase encountered when Y. lipolytica was cultivated in synthetic culture media containing high concentrations of glycerol. Therefore, by enriching with 0.3% yeast extract the synthetic culture medium containing 15% glycerol, we could cultivate Y. lipolytica up to 83 g/L dry cell weight in a batch culture. Furthermore, over 100 g/L and 88 units/mL of rice alpha-amylase activity were obtained in less than 50 h with a one-step feeding process in which a recombinant Y. lipolytica expressing rice alpha-amylase was cultivated in the 10% glycerol medium enriched with 0.3% yeast extract and fed only once with the concentrated feeding medium (60% glycerol). The easy cultivation of recombinant Y. lipolytica to a high cell density may strengthen its position as a host for heterologous protein production.     

Catalase effect on cell death for the improvement of recombinant protein production in baculovirus-insect cell system

Baculovirus expression vector system (BEVS) in host insect cells is a powerful technology to produce recombinant proteins, as well as virus-like particles (VLP). However, BEVS is based on baculovirus infection, which limits the recombinant protein production by inducing insect cell death. Herein a new strategy to enhance cell life span and to increase recombinant protein production was developed. As baculovirus infection induces cellular oxidative stress, the ability of several antioxidants to inhibit cell death was tested during infection. The production of rotavirus structural proteins was used as model to analyse this new strategy. We found that only catalase is able to partially prevent cell death triggered by baculovirus infection and to inhibit lipid peroxidation. An increase in recombinant protein production was coupled with the partial cell death inhibition. In summary, the addition of catalase is a promising strategy to improve recombinant protein production in BEVS, by delaying insect cell death.     

A novel control scheme for inducing angiostatin-human IgG fusion protein production using recombinant CHO cells in a oscillating bioreactor

In this study, a novel control scheme for inducing protein production using a recombinant CHO cell line in a BelloCell bioreactor was developed. This control scheme was applied in a simple regular semi-batch process. Production of angiostatin-human IgG fusion protein in a suspension recombinant CHO cell culture and a protein-free medium was used for this study. The bottom holding time (BH) was the sole operating variable to control the exposure time of the cells immobilized on the carriers to the air and allow the nutrient remained on the liquid film of the carriers to be consumed to a threshold level so that the cells can be arrested and promoted for protein production. In the cell cultures with various BH (1.5-90 min), final cell densities of 1.6-4.0 x 10(9) have been obtained in 20 days while total angiostatin-human IgG production of 228-388 mg have been harvested. In general, low BH will minimize the nutrient limitation and favor the cell growth, while high BH will restrict the nutrient and promote the production in this type of non-growth associated production systems. It was found that specific production rate was generally inversely proportional to the specific growth rate. In this case of study, BH of 30 and 60 min were found to be about 72% better than BH of 1.5 min and 35% better than BH of 9 and 90 min in term of the total angiostatin-human IgG production. In comparison to a conventional spinner flask study, a 3.8-fold increase of the total angiostatin-human IgG production was realized in a 35-day culture. This study illustrated that a simple method of using BH in a semi-batch process can effectively control the apparent nutrient concentration to the cells, and thus regulate the cell growth and protein production in a novel oscillating bioreactor.     

Membrane anchored protein production from spheroid, porous, and solid microcarrier chinese hamster ovary cell cultures

The influence of the microcarrier type on the performance of a controlled release process used to produce a recombinant glycosyl-phosphatidylinositol anchored protein was investigated. Chinese hamster ovary (CHO) cells expressing the human melanoma tumor antigen (p97) were cultured in 10% serum on Cultispher-GH porous microcarriers and then, for protein production, maintained in 2% serum. Cells were harvested every 48 h and p97 was recovered at 90 mug/mL and 40% purity. Harvested p97 concentrations were increased by harvestingfrom spheroid (241 mug/mL) and smaller porous microcarrier, Cultispher-G (167 mug/mL) cultures. The low total cell specific p97 production of cells cultured on Cultispher-GH was due to necrosis of cells within the beads, decreased p97 expression of the immobilized cells, dilution by the liquid (up to 40% volume) associated with settled beads, and incomplete recovery of p97 from within the beads. Cells cultured on solid microcarriers, Cytodex-1, had the highest cell viability and cell specific p97 production, It is recommended that a two-stage cyclic harvesting process of cells cultured on small Cultispher-G or on Cytodex-1 beads would minimize protein loss and maximize cell specific protein recovery. (c) 1995 John Wiley & Sons Inc.     

微囊化重组CHO细胞制备和培养条件的优化

微囊化重组基因细胞移植治疗肿瘤是一种新兴的肿瘤基因治疗方法,然而由于目前微囊化细胞规模化制备和培养技术还不成熟,阻碍了其在临床治疗中的推广与应用。以重组CHO细胞为模型,考察了不同的微囊制备和培养条件对微囊化细胞生长和内皮抑素表达的影响。实验表明,种子细胞所处的生长阶段和细胞接种密度对微囊化细胞生长和内皮抑素表达的影响较大,对数生长期的细胞进行包囊并且细胞接种密度为1×106~2×106cells/mL微囊时微囊内细胞生长良好、内皮抑素表达量高。微囊制备时间对细胞活性和内皮抑素表达也有较大的影响,制备时间延长对细胞的损伤增大,因此制备时间应控制在5h以内。生物微胶囊在制备过程中会造成细胞损伤,而体外培养是恢复细胞活性的良好方法,在培养过程中微囊接种量为5%时对细胞生长和内皮抑素表达有利。     

Secreted human apolipoprotein(a) kringle IV-10 and kringle V inhibit angiogenesis and xenografted tumor growth

Abstract Angiogenesis plays an important role in normal physiology of blood vessel growth, but can contribute to the pathogenesis of diseases, such as cancer. A new anti-angiogenic recombinant kringle protein, composed of the fused domains of human apolipoprotein(a) carboxyl-terminal kringle IV-10 and kringle V, was expressed in Pichia pastoris and human colorectal carcinoma (HCT 116) cells to investigate its influence on angiogenesis and tumor growth. The mature recombinant protein exhibited the characteristic features of kringle-containing proteins (glycosylation and disulfide bond formation) and, when added to cultures of human umbilical vein endothelial cell, resulted in a 31% decrease in proliferation relative to untreated controls (p<0.05). The neo-angiogenesis was diminished by 63% in chick embryos treated with 10 mug recombinant protein compared with 7% for phosphate buffer solution-treated embryos (p<0.01). Transfection of a kringle IV-10-kringle V fusion protein construct into HCT 116 cells decreased tumorigenesis and inhibited tumor growth in vivo without affecting tumor cell proliferation. HCT 116 cells that expressed recombinant protein displayed a much lower relative growth ratio of 8% (p<0.01) against the control tumor cells. From these results, we conclude that human apolipoprotein(a) carboxyl-terminal kringle IV-10-kringle V fusion protein is an effective inhibitor of angiogenesis and angiogenesis-dependent tumor growth.     

A rational approach to improving productivity in recombinant Pichia pastoris fermentation

A Mut(S) Pichia pastoris strain that had been genetically modified to produce and secrete sea raven antifreeze protein was used as a model system to demonstrate the implementation of a rational, model-based approach to improve process productivity. A set of glycerol/methanol mixed-feed continuous stirred-tank reactor (CSTR) experiments was performed at the 5-L scale to characterize the relationship between the specific growth rate and the cell yield on methanol, the specific methanol consumption rate, the specific recombinant protein formation rate, and the productivity based on secreted protein levels. The range of dilution rates studied was 0. 01 to 0.10 h(-1), and the residual methanol concentration was kept constant at approximately 2 g/L (below the inhibitory level). With the assumption that the cell yield on glycerol was constant, the cell yield on methanol increased from approximately 0.5 to 1.5 over the range studied. A maximum specific methanol consumption rate of 20 mg/g. h was achieved at a dilution rate of 0.06 h(-1). The specific product formation rate and the volumetric productivity based on product continued to increase over the range of dilution rates studied, and the maximum values were 0.06 mg/g. h and 1.7 mg/L. h, respectively. Therefore, no evidence of repression by glycerol was observed over this range, and operating at the highest dilution rate studied maximized productivity. Fed-batch mass balance equations, based on Monod-type kinetics and parameters derived from data collected during the CSTR work, were then used to predict cell growth and recombinant protein production and to develop an exponential feeding strategy using two carbon sources. Two exponential fed-batch fermentations were conducted according to the predicted feeding strategy at specific growth rates of 0.03 h(-1) and 0.07 h(-1) to verify the accuracy of the model. Cell growth was accurately predicted in both fed-batch runs; however, the model underestimated recombinant product concentration. The overall volumetric productivity of both runs was approximately 2.2 mg/L. h, representing a tenfold increase in the productivity compared with a heuristic feeding strategy.     

Enhanced expression of various exogenous genes in recombinant Chinese hamster ovary cells in presence of dimethyl sulfoxide

Dimethyl sulfoxide (DMSO) (1% v/v) stimulated stable transformed Chinese hamster ovary (CHO) cells to synthesize different recombinant proteins and repress their proliferation rate. The expressions of a fusion protein and -galactosidase were increased 1.6- and 1.4-fold after adding DMSO. The expression of fusion protein was increased by up to 2.8-fold that of uninduced control by the simultaneous addition of DMSO and pentanoic acid. However, DMSO did not increase the production of the monoclonal antibody (immunoglobulin G) of three hybridoma cell lines (OKM1, OKT4 and HyGPD-YK-1-1), although it could inhibit the growth rates of the hybridoma.     

A novel feeding strategy for enhanced protein production by fed-batch fermentation in recombinant Pichia pastoris

A novel feeding strategy for enhanced protein production of hepatitis B virus surface antigen (HBsAg) in fed-batch fermentation, recombinant Pichia pastoris, has been developed. A minimal salt medium was used to grow cells in the initial batch fermentation, followed by a glycerol+salts fed-batch phase. At the end of the fed-batch phase a dry cell weight of 130 g l⁻¹ was achieved. In the absence of basal salts, the same amount of glycerol feed resulted in only 90 g l⁻¹ cell dry weight. When a limited amount of casamino acids were also included every 24 h during methanol induction, there was a two-fold increase in expression levels of HBsAg. After 192 h of induction, the expression levels of HBsAg (soluble and insoluble) reached >1 g l⁻¹ using the Mut⁻ strain. Thus, the use of basal salts in the glycerol feed, along with the addition of limited amounts of casamino acids with the methanol feed, resulted in an increased expression of total HBsAg.