Effect of environmental conditions on the expression levels of a recombinant 11S amaranth globulin in Escherichia coli

The expression in Escherichia coli strain Rosetta of the recombinant acidic subunit from the 11S amaranth seed storage protein (protein ACM3) was studied at flask and at bioreactor levels. This subunit was modified by inserting four Val-Tyr antihypertensive peptides in tandem into its third variable region and also with the tripeptide Ile-Pro-Pro in the Cterminal region. Flasks experiments allowed us to define the best conditions for the preparation and expression and accumulation of the protein ACM3, including the certainty of its presence within the cells especially as an insoluble fraction. The effects of cultivation temperature, aeration rate and agitation speed on the production of the protein ACM3 was tested in a 5-L batch bioreactor. Applying response surface methodology (RSM) we found that the aeration rate was the most significant factor affecting in a positively way the production yields and productivity of the recombinant protein. Temperature had effect only in conjunction to aeration. The highest recombinant acidic subunit concentration (747 mg L-1) and the highest productivity (186 mg L-1 h-1) were attained in 4 h of cultivation when the factors evaluated were controlled at its central values: 0.1 vvm, 300 rpm, and 30.5° C. Results from this study indicate that RSM is an effective technique to maximize the production of this recombinant protein.     

基于响应面分析方法的钩端螺旋体三联属特异性蛋白抗原原核表达条件的优化

脂蛋白LipL32和LipL21及穿膜蛋白OMPL1是问号钩端螺旋体(简称钩体)属特异性表面抗原,可作为通用型钩体基因工程疫苗抗原.[目的]在我们的研究中,为了获得使得重组人工融合基因lipL32/1-lipL21-ompL1/2获得较高的表达水平,我们优化了重组宿主大肠杆菌的表达条件.[方法]我们采用了基于中心复合设计(CCD)的响应面分析方法(RSM).影响重组大肠杆菌生长的主要因素包pH、诱导剂IPTG浓度、诱导前培养实践、诱导时间以及诱导温度.响应面分析方法可以从这些因素中找到适合目的蛋白表达的最优表达条件.[结果]我们的结果显示在pH7.9、0.20mmol/LIPTG、诱导前培养时间2.5 h、诱导时间5.83 h、诱导后温度31℃条件下,可获得目的重组蛋白37.78 mg/L的最大表达量.[结论]实验结果表明采用基于中心复合设计的响应面分析方法能够较吹靥岣吣康牟锏牟?利用统计方法不但可以减少试验的次数,而且还能够从影响蛋白的因素中找出最重要的影响因素,因此该方法不仅对重组蛋白表达条件的优化有用,而且是一种很好的筛选方法.     

Utilization of chicory roots for microbial endoinulinase production

AIMS: The optimal culture conditions for endoinulinase production using chicory roots were studied in shake-flask culture. METHODS AND RESULTS: Much higher enzyme production was achieved with Xanthomonas sp. (15 U ml(-1)) than with Pseudomonas sp. (3 U ml(-1)). Optimized culture conditions of Xanthomonas sp. for endoinulinase production in flask culture were: chicory powder, 5 g l(-1); temperature, 37 degrees C; pH, 7.0; agitation speed, 100 rev min(-1). CONCLUSION: Maximum bacterial growth and enzyme production were 6.2 g l(-1) and 20 U ml(-1) under optimal conditions, respectively. SIGNIFICANCE AND IMPACT OF THE STUDY: Chicory roots could be used as a fermentation substrate for the production of enndoinulinase.     

Dependence of morphology on agitation intensity in fed-batch cultures of Aspergillus oryzae and its implications for recombinant protein production

We previously reported that, although agitation conditions strongly affected mycelial morphology, such changes did not lead to different levels of recombinant protein production in chemostat cultures of Aspergillus oryzae (Amanullah et al., 1999). To extend this finding to another set of operating conditions, fed-batch fermentations of A. oryzae were conducted at biomass concentrations up to 34 g dry cell weight/L and three agitation speeds (525, 675, and 825 rpm) to give specific power inputs between 1 and 5 kWm(-3). Gas blending was used to control the dissolved oxygen level at 50% of air saturation except at the lowest speed where it fell below 40% after 60-65 h. The effects of agitation intensity on growth, mycelial morphology, hyphal tip activity, and recombinant protein (amyloglucosidase) production in fed-batch cultures were investigated. In the batch phase of the fermentations, biomass concentration, and AMG secretion increased with increasing agitation intensity. If in a run, dissolved oxygen fell below approximately 40% because of inadequate oxygen transfer associated with enhanced viscosity, AMG production ceased. As with the chemostat cultures, even though mycelial morphology was significantly affected by changes in agitation intensity, enzyme titers (AGU/L) under conditions of substrate limited growth and controlled dissolved oxygen of >50% did not follow these changes. Although the measurement of active tips within mycelial clumps was not considered, a dependency of the specific AMG productivity (AGU/g biomass/h) on the percentage of extending tips was found, suggesting that protein secretion may be a bottle-neck in this strain during fed-batch fermentations.     

纳豆激酶液态发酵条件的研究

考察纳豆杆菌在7.5 L发酵罐中分批发酵产纳豆激酶的条件,纳豆激酶酶活采用四肽底物测定。结果表明:纳豆杆菌生长和产酶的适宜条件不一致。发酵过程中发酵罐搅拌转速控制为500 r/min不变,0～12 h时控制pH为8.0、温度为37℃;12～36 h调整pH为7.0、温度为30℃;16 h时补加外源C源,连续发酵36 h。该过程中发酵液中比酶活最高达到3 232 U/mL,与摇瓶发酵相比,比酶活提高了58%。     

Production of recombinant protein using the HeLa S3-vaccinia virus expression system: bioreactor perfusion and effects of post-infection temperature

Adaptation of the vaccinia virus expression system to HeLa S3 suspension bioreactor culture for the production of recombinant protein was conducted. Evaluation of hollow fiber perfusion of suspension culture demonstrated its potential for increased cell density prior to infection. The hollow fiber was also used for medium manipulations prior to infection. Two process parameters, multiplicity of infection (MOI) and temperature during the protein production phase, were evaluated to determine their effect on expression of the reporter protein, enhanced green fluorescent protein (EGFP). An MOI of 1.0 was sufficient for infection and led to the highest level of intracellular EGFP expression. Reducing the temperature to 34 degrees C during the protein production phase increased production of the protein two-fold compared to 37 degrees C in spinner flask culture. Scaling up the process to a 1.5-liter bioreactor with hollow fiber perfusion led to an overall production level of 9.9 microg EGFP/10(6) infected cells, or 27 mg EGFP per liter.     

The role of aeration and agitation in the production of glucose oxidase in submerged culture

The influence of agitation and aeration on growth and on production of glucose oxidase of Asp. niger has been studied. It was found that both rate of growth and glucose oxidase production was higher at an agitation speed of 700 rpm than at 460 rpm. Further increase in speed of agitation resulted in neither a higher rate of growth nor a higher glucose oxidase activity. Total glucose oxidase activity was highest in a medium containing 5% sugar (at an agitation speed of 700 rpm) and did not get higher when the sugar concentration of the medium was increased to 7%. When pure oxygen was bubbled through the culture the rate of growth of the culture (in the linear phase) was 95 mg. mycelial dry wt./100 ml./hr., and only 61 mg. when air was applied. The glucose oxidase activity of oxygenated culture was double the activity of aerated culture. Viscosity of the homogenized culture became higher with higher concentration of mycelia. The viscosity of oxygenated culture was found to be lower than that of aerated culture.     

Effect of aeration and agitation on the production of mycelial biomass and exopolysaccharides in an enthomopathogenic fungus Paecilomyces sinclairii

AIMS: The objective of the present study was to investigate the influence of aeration rate and agitation intensity on the production of mycelial biomass and exopolysaccharide (EPS) in Paecilomyces sinclairii. METHODS AND RESULTS: The P. sinclairii was cultivated under various aeration and agitation conditions in a 5 l stirred-tank bioreactor. The highest mycelial biomass (30.5 g l-1) and EPS production (11.5 g l-1) were obtained at a high aeration rate (3.5 v.v.m.) and at a high agitation speed (250 rev min-1). The apparent viscosities (6000-8000 cP) of fermentation broth increased rapidly towards the end of fermentations at high aeration and agitation conditions. CONCLUSIONS: The high level of dissolved oxygen achieved at a high aeration rate (3.5 v.v.m.) associated with higher hyphal density eventually resulted in enhanced EPS production. Agitation intensity was also proved to be a critical factor influencing on both the mycelial biomass and EPS production: high agitation speeds up to 250 rev min-1 were preferred to the yields of biomass and EPS production. SIGNIFICANCE AND IMPACT OF THE STUDY: The critical effects of aeration and agitation in the culture process of P. sinclairii were found, which is widely applicable to other kinds of basidiomycetes or ascomycetes in their submerged culture processes.     

Cultivation of Methylosinus trichosporium OB3b: III. production of particulate methane monooxygenase in continuous culture

Continous culture experiments with the obligatory methanotroph, Methylosinus trichosporium OB3b, were conducted to study the whole-cell methane monooxygenase (MMO) and nitrogenase activities in a nitrate minimal salts medium under oxygen-limited conditions with methane as the carbone source. The important variables investigated were the feed medium concentrations of copper and nitrate, CO(2) addition, the agitation speed, and the dilution rate. M. trichosporium OB3b required quantitative amounts of copper (2.6 x 10(-4) g Cu/g dry cell Wt) for the exclusive production of particulate MMo during continous culture growth. When the feed medium nitrate concentration was varied in the range of 5-50 mM, the whole-cell specific pMMO activity exhibited a maximum at 40 mM. The elimination of external CO(2) gassing decreased pMMO activity by more than 30%. The steady-state cell density increased continuously over a 300-700 rpm range of agitation speed, whereas, the pMMO activity became maximal at 400 rpm. Also, the pMMO activity increased with the dilution rate up to 0.06 h(-1) and remained constant thereafter. Maximal continuous pMMO productivity was, thus, achieved in Higgin's medium containing 10 muM Cu, 80 muM Fe, and 40 mM nitrate with an agitation speed of 500 rpm and a dilution rate of 0.06 h(-1). Nitrogenase activity, on the other hand, increased over a feed medium copper concentration of 2-15 muM, falling sharply at 20 muM, and it exhibited a minimum at 20 mM when the feed medium nitrate concentration was varied. (c) 1992 John Wiley & Sons, Inc.     

Comparison of biotin production by recombinant Sphingomonas sp. under various agitation conditions

Biotin production by fermentation of recombinant Sphingomonas sp./pSP304 was investigated. A complex medium containing 60g/l of glycerol and 30g/l of yeast extract was suitable for biotin production. Biotin was produced in the late logarithmic or stationary phase after glycerol starvation. The optimum pH value for biotin production was 7.0. When the dissolved oxygen concentration (DO) was controlled at a constant level, the biotin concentration produced after 120h was significantly lower than that obtained in a test tube culture. Therefore, a batchwise jar-fermentor culture with a constant agitation speed and without DO control was conducted for investigating the effect of agitation conditions on biotin production. Six types of impeller were tested: turbine-blade type, turbo-lift type, rotating mesh type (EGSTAR((R))), screw with draft tube type, Maxblend((R))type, and anchor type. With some impellers, agitation speed was also changed. Both the maximum cell concentration and biotin production varied depending on agitation conditions. Relatively high cell concentrations were attained with four of the impeller types, turbine-blade type, rotating mesh type, Maxblend((R)) type, and anchor type. Among these impellers, the turbine-blade impeller with sintered sparger was suitable for biotin production. After 120h, the cell concentration reached an OD(660) of 43 and a biotin concentration of 66mg/l was obtained, which was comparable with the results from the test tube culture. Morphological variation was also observed depending on the agitation conditions: oval-shaped, rod-shaped, and elongated-shaped cells. Biotin production was relatively high in slightly long rod-shape cells but low in elongated cells. The difference in morphology appeared to depend on the shear stress. It was found that biotin production was strongly correlated with cell length and the oxygen transfer coefficient (k(L)a); cell lengths in the range 4-7μm and k(L)a values in the range 1.5-2.0/min were found to be suitable for biotin production in jar-fermentor culture.     

Comparison of growth and recombinant protein expression in two different insect cell lines in attached and suspension culture

Culture conditions required for obtaining maximum recombinant protein concentrations from two cell lines, Spodoptera frugiperda (IPLBeta-Sf21-AE) and Trichoplusia ni (Tn 5Beta-1-4), were determined in this work. Conditions studied include mode of culture (suspended vs attached), agitation rates, inoculum sizes, cell concentration at the time of infection, and various serum-free media (SFM). Results were compared with the performance of attached cultures in TnM-FH with 10% fetal bovine serum. Growth rates in the different culture media tested were similar, but the cell numbers achieved (i.e., yield) improved 2 to 2.7-fold in SFM over cultures in TnM-FH. Agitation rates of 150-160 rpm were necessary for maximum growth of suspended Tn 5Beta-1-4 cells compared to 125-150 rpm for Sf-21 cells. An inoculum size of 5 x 10(5) cells/mL gave good growth rates and optimum biomass yields for both cell lines. Cultures of both cell lines were infected with viruses encoding for beta-galactosidase or human secreted alkaline phosphatase (seAP). Protein expression in TnM-FH in attached culture showed that Tn 5Beta-1-4 cells are 2-4.5 times more productive on a per cell basis than Sf-21 cells grown under similar conditions. Production of beta-galactosidase in Sf-21 cells increased 50% in suspension cultures with SFM compared to attached cultures in TnM-FH, but seAP expression was essentially unchanged by culture techniques. The Tn 5Beta-1-4 cells produced 2.6-4.4 and 2.7-3 times more beta-galactosidase and seAP, respectively, in SFM in suspension compared to Sf-21 cells. EX-CELL 401 and Sf900-II were formulated as optimized SFM for Sf cell lines. However, in Sf-21 cultures EX-CELL 400 performed better than the other two media, as it increased the beta-galactosidase yield up to 25%. Surprisingly, EX-CELL 401 was the best medium for the production of beta-galactosidase by Tn 5Beta-1-4 cells, resulting in 25% and 69% higher volumetric and specific yields, respectively, compared to EX-CELL 405 which was formulated for this specific cell line. These results show that even when culture media are designed for maximal growth of a specific cell line, other media may provide the best conditions for protein production.     

Effects of agitation intensity on mycelial morphology and protein production in chemostat cultures of recombinant Aspergillus oryzae

The effects of agitation on fragmentation of a recombinant strain of Aspergillus oryzae and its consequential effects on protein production have been investigated. Constant mass, 5.3-L chemostat cultures at a dilution rate of 0.05 h-1 and a dissolved oxygen level of 75% air saturation, have been conducted at 550, 700, and 1000 rpm. These agitation speeds were chosen to cover a range of specific power inputs (2.2 to 12 kW m-3) from realistic industrial levels to much higher values. The use of a constant mass chemostat linked to a gas blender allowed variation of agitation speed and hence gas hold-up without affecting the dilution rate or the concentration of dissolved oxygen. The morphology of both the freely dispersed mycelia and clumps was characterized using image analysis. Statistical analysis showed that it was possible to obtain steady states with respect to morphology. The mean projected area at each steady state under growing conditions correlated well with the 'energy dissipation/circulation" function, [P/(kD3tc)], where P is the power input, D the impeller diameter, tc the mean circulation time, and k is a geometric constant for a given impeller. Rapid transients of morphological parameters in response to a speed change from 1000 to 550 rpm probably resulted from aggregation. Protein production (alpha-amylase and amyloglucosidase) was found to be independent of agitation speed in the range 550 to 1000 rpm (P/V = 2.2 and 12.6 kW m-3, respectively), although significant changes in mycelial morphology could be measured for similar changes in agitation conditions. This suggests that mycelial morphology does not directly affect protein production (at a constant dilution rate and, therefore, specific growth rate). An understanding of how agitation affects mycelial morphology and productivity would be valuable in optimizing the design and operation of large-scale fungal fermentations for the production of recombinant proteins. Copyright 1999 John Wiley & Sons, Inc.     

Production of hantavirus Puumala nucleocapsid protein in Saccharomyces cerevisiae for vaccine and diagnostics

The production of hantavirus Puumala nucleocapsid (N) protein for potential applications as a vaccine and for diagnostic purposes was investigated with Saccharomyces cerevisiae as a recombinant host. The N protein gene and the hexahistidine tagged N (h-N) protein gene were expressed intracellular from a 2-microm plasmid vectors under the control of a fused galactose inducible GAL10-PYK promoter. For monitoring the recombinant gene expression, a h-N and a GFP fusion protein was used. Different cultivation strategies and growth media compositions were tested in shake flasks and a 5 l bioreactor. When using defined YNB growth medium, we found the biomass yield to be unsatisfactorily low. Higher concentrated YNB medium, promoted cell growth but showed a pronounced inhibitory effect on heterologous gene expression. This phenomenon could not be attributed to plasmid losses, as we could demonstrate high stability of the vector under the applied cultivation conditions. Supplementation of YNB medium with extracts of plant origin resulted in increased biomass yields with concomitant high expression levels of the recombinant gene. The modified medium was used for fed-batch cultivations where basic metabolic features as well as growth parameters were determined in addition to recombinant gene expression. The maximal volumetric yield of N protein was 316 mg l(-1), the respective yield of h-N protein was 284 mg l(-1). Our study provides a basis for large-scale production of hantavirus vaccines, which satisfies economic efficiency as well as biosafety regulations for human applications.     

Rhamnolipid production by Pseudomonas aeruginosa engineered with the Vitreoscilla hemoglobin gene

The potential of Pseudomonas aeruginosa expressing the Vitreoscilla hemoglobin gene (vgb) for rhamnolipid production was studied. P. aeruginosa (NRRL B-771) and its transposon mediated vgb transferred recombinant strain, PaJC, were used in the research. The optimization of rhamnolipid production was carried out in the different conditions of cultivation (agitation rate, the composition of culture medium and temperature) in a time-course manner. The nutrient source, especially the carbon type, had a dramatic effect on rhamnolipid production. The PaJC strain and the wild type cells of P. aeruginosa started producing biosurfactant at the stationary phase and its concentration reached maximum at 24 h (838 mg/l(-1)) and at 72 h (751 mg l(-1)) of the incubation respectively. Rhamnolipid production was optimal in batch cultures when the temperature and agitation rate were controlled at 30 degrees C and 100 rpm. It reached 8373 mg l(-1) when the PaJC cells were grown in 1.0% glucose supplemented minimal media. Genetic engineering of biosurfactant producing strains with vgb may be an effective method to increase its production.     

Control of culture environment for improved polyethylenimine-mediated transient production of recombinant monoclonal antibodies by CHO cells

In this study we describe optimization of polyethylenimine (PEI)-mediated transient production of recombinant protein by CHO cells by facile manipulation of a chemically defined culture environment to limit accumulation of nonproductive cell biomass, increase the duration of recombinant protein production from transfected plasmid DNA, and increase cell-specific production. The optimal conditions for transient transfection of suspension-adapted CHO cells using branched, 25 kDa PEI as a gene delivery vehicle were experimentally determined by production of secreted alkaline phosphatase reporter in static cultures and recombinant IgG4 monoclonal antibody (Mab) production in agitated shake flask cultures to be a DNA concentration of 1.25 microg 10(6) cells(-1) mL(-1) at a PEI nitrogen:DNA phosphate ratio of 20:1. These conditions represented the optimal compromise between PEI cytotoxicity and product yield with most efficient recombinant DNA utilization. Separately, both addition of recombinant insulin-like growth factor (LR3-IGF) and a reduction in culture temperature to 32 degrees C were found to increase product titer 2- and 3-fold, respectively. However, mild hypothermia and LR3-IGF acted synergistically to increase product titer 11-fold. Although increased product titer in the presence of LR3-IGF alone was solely a consequence of increased culture duration, a reduction in culture temperature post-transfection increased both the integral of viable cell concentration (IVC) and cell-specific Mab production rate. For cultures maintained at 32 degrees C in the presence of LR3-IGF, IVC and qMab were increased 4- and 2.5-fold, respectively. To further increase product yield from transfected DNA, the duration of transgene expression in cell populations maintained at 32 degrees C in the presence of LR3-IGF was doubled by periodic resuspension of transfected cells in fresh media, leading to a 3-fold increase in accumulated Mab titer from approximately 13 to approximately 39 mg L(-1). Under these conditions, Mab glycosylation at Asn297 remained essentially constant and similar to that of the same Mab produced by stably transfected GS-CHO cells. From these data we suggest that the efficiency of transient production processes (protein output per rDNA input) can be significantly improved using a combination of mild hypothermia and growth factor(s) to yield an extended "activated hypothermic synthesis".     

Effects of dissolved oxygen tension and agitation rate on the production of heat-shock protein glycoprotein 96 by MethA tumor cell suspension culture in stirred-tank bioreactors

Heat-shock protein glycoprotein (gp96) serves as a natural adjuvant for chaperoning antigenic peptide into the immune surveillance pathway. In our laboratory, MethA tumor cell suspension culture process has been recently developed for gp96 production in spinner flask. In this work, effects of dissolved oxygen tension (DOT) and agitation rate on this process were studied in stirred-tank bioreactor. The optimal conditions for gp96 production were different with those for MethA tumor cell growth. MethA tumor cell growth pattern was not much changed by various levels of DOT and agitation rate, while gp96 biosynthesis was more sensitive to DOT and agitation rate. Compared with 50% of DOT, the production and specific productivity of gp96 was increased by 27 and 66% at 10% of DOT, respectively. Compared with the agitation rate of 100 rpm, the production and volumetric productivity of gp96 was increased by 48 and 144% at the agitation rate of 200 rpm, respectively. Low DOT (i.e., 10% of air saturation) and high agitation rate (i.e., 200 rpm) were identified to be favorable for gp96 biosynthesis. The results of this work might be useful to scale-up the bioprocess into the pilot scale.     

Impact of dissolved oxygen concentration on some key parameters and production of rhG-CSF in batch fermentation

The impact of different levels of agitation speed, carbondioxide and dissolved oxygen concentration on the key parameters and production of rhG-CSF in Escherichia coli BL21(DE3)PLysS were studied. Lower carbondioxide concentrations as well as higher agitation speeds and dissolved oxygen concentrations led to reduction in the acetate concentrations, and enhanced the cell growth, but inhibited plasmid stability and rhG-CSF expression. Similarly, higher carbondioxide concentrations and lower agitation speeds as well as dissolved oxygen concentrations led to enhanced acetate concentrations, but inhibited the cell growth and protein expression. To address the bottlenecks, a two-stage agitation control strategy (strategy-1) and two-stage dissolved oxygen control strategy (strategy-2) were employed to establish the physiological and metabolic conditions, so as to improve the expression of rhG-CSF. By adopting strategy-1 the yields were improved 1.4-fold over constant speed of 550 rpm, 1.1-fold over constant dissolved oxygen of 45%, respectively. Similarly, using strategy-2 the yields were improved 1.6-fold over constant speed of 550 rpm, 1.3-fold over constant dissolved oxygen of 45%, respectively.     

Solasodine production from cell culture of <Emphasis Type="Italic">Solanum hainanense</Emphasis> Hance

Stem explants of Solanum hainanense Hance plantlets were cultured on Murashige and Skoog solid medium, containing 3% (w/v) sucrose, supplemented with 0.1 mg/L benzylaminopurine (BAP) and 1.0 mg/L 2, 4-dichlorophenoxyacetic acid (2, 4-D) for callus production. To establish the cell suspension culture, 3 g of fresh callus were cultured in 50 mL of the same medium, but without a solid agent, at an agitation speed of 120 rpm. Every 15 mL of culture was sub-cultured in fresh MS liquid medium for maintenance. The cell biomass of S. hainanense reached a maximum value of 18.47 g after 4 weeks of culture on the same MS medium, but with the sucrose content increased to 4%, at an agitation speed of 150 rpm, with 20 mL of inoculum. Analysis via high performance liquid chromatography (HPLC) showed that the solasodine content in the cell suspension after 4-weeks old (121.01 mg/g) was higher than that of in planta 1-year old roots (20.52 mg/g) by approximately 6-fold.     

Use of moving aeration membrane bioreactor for the efficient production of tissue type plasminogen activator in serum free medium

A moving aeration-membrane (MAM) bioreactor was employed for the production of 2 μg/mL of tissue type Plasminogen Activator (tPA) in serum free medium from normal human fibroblast cells. This system could maintain high cell density for long periods of steady state conditions in perfusion cultivation. Under normal operating conditions, shear stress was as low as 0.65 dynes/cm² at the agitation speed of 80 rpm. Even though cell density gradually decreased with increasing agitation speed, tPA production increased linearly with increasing shear stress within a moderate range. This culture system allowed production of 2 μg tPA/mL while maintaining a high cell density of 1.0×10⁷ viable cells/mL.