Expression kinetics and plasmid stability of recombinant E. coli encoding urease-derived peptide with bioinsecticide activity

The nucleotide sequence encoding for an insecticidal peptide derived from the Canavalia ensiformis urease gene jbureII (AF 468788), was cloned and expressed in the pET101/Escherichia coli expression system. Bacterial cultivation in shaker with lactose as inducer produced 1.26 μg of recombinant peptide/mg protein, after 8 h of growth. The plasmid stability and the expression of the recombinant peptide were studied in bioreactor. Expression of the recombinant peptide was strongly affected by pH of cultures, with a decrease of more than 50% when acidification was freely allowed. Likewise, peptide production and plasmid stability were shown to be affected by aeration and agitation speed, both decreasing for higher values of oxygen mass transfer rates. Despite these difficulties, in bioreactor cultures carried out with controlled pH, low oxygen mass transfer rates and using lactose as inducer, we were able to achieve a total peptide production of 7.14 μg/mg protein, which represents approximately 2% of total cell protein. Bioassays were carried out using the purified peptide on insect models. The peptide fed to Dysdercus peruvianus nymphs produced 100% mortality after 11 days, deaths starting with a lag phase of 3–4 days, confirming that the bioreactor-produced peptide retained its biological activity.     

Improvement of Panax notoginseng cell culture for production of ginseng saponin and polysaccharide by high density cultivation in pneumatically agitated bioreactors

A Panax notoginseng cell culture was successfully scaled up from shake flask to 1.0-L bubble column reactor and concentric-tube airlift reactor. High-density bioreactor batch cultivation was carried out using a modified MS medium. The maximum cell density in batch cultures reached 20.1, 21.0 and 24.1 g/L in the shake flask, bubble column and airlift reactors, respectively, and their corresponding biomass productivity was 950, 1140 and 1350 mg/(L x d) for each. The productivity of ginseng saponin was 70, 96 and 99 mg/(L x d) in the flask, bubble column and airlift reactors, respectively; and the polysaccharide productivity reached 104, 119 and 151 mg/(L x d) for each. Furthermore, a fed-batch cultivation strategy was developed on the basis of specific oxygen uptake rate (SOUR), i.e., sucrose feeding before a sharp decrease of SOUR, and the highest cell density of 29.7 g/L was successfully achieved in the airlift bioreactor on day 17 with a very high biomass productivity of 1520 mg/(L x d). The concentrations of ginseng saponin and polysaccharide reached about 2.1 and 3.0 g/L, respectively, and their productivity was 106 (saponin) and 158 mg/(L x d) (polysaccharide). This work successfully demonstrated the high-density bioreactor cultivation of P. notoginseng cells in pneumatically agitated bioreactors and the reproduction of the shake flask culture results in bioreactors. The cell density, biomass productivity, production titer and productivity of both ginseng saponin and polysaccharide obtained here were the highest that have been reported on a reactor scale for all the ginseng species.     

Short Communication: Effect of agitation rate on the growth and production of xylanase free of cellulase by Thermomyces lanuginosus MH4 in bioreactor

Cellulase-free xylanase production by T. lanuginosus MH4 was investigated in a 3-litre stirred tank bioreactor under different agitation rates and an aeration rate of 1v/v/m. The cultivation time in the bioreactor was reduced significantly over that in shake culture conditions. A xylanase productivity of 0.1 mkat1–1h–1 was achieved on xylan in the bioreactor. This was nearly double to that obtained in shake culture. The agitation rates influenced both growth and enzyme secretion in the bioreactor. The highest level of biomass concentration and activities of both xylanase and -xylosidase were obtained at 150 revmin–1     

Production of carbonyl reductase by Geotrichum candidum in a laboratory scale bioreactor

Fungal fermentation is very complex in nature due to its nonlinear relationship with the time, especially in batch culture. Growth and production of carbonyl reductase by Geotrichum candidum NCIM 980 have been studied in a laboratory scale stirred tank bioreactor at different pH (uncontrolled and controlled), agitation, aeration and dissolved oxygen concentration. The yield of the process has been calculated in terms of glucose consumed. Initial studies showed that fermenter grown cells have more than 15 times higher activity than that of the shake flask grown cells. The medium pH was found to have unspecific but significant influence on the enzyme productivity. However, at controlled pH 5.5 the specific enzyme activity was highest (306U/mg). Higher agitation had detrimental effect on the cell mass production. Dissolved oxygen concentration was maintained by automatic control of the agitation speed at an aeration rate of 0.6 volume per volume per minute (vvm). Optimization of glucose concentration yielded 21g/l cell mass with and 9.77x10(3)U carbonyl reductase activity/g glucose. Adaptation of different strategies for glucose feeding in the fermenter broth was helpful in increasing the process yield. Feeding of glucose at a continuous rate after 3h of cultivation yielded 0.97g cell mass/g glucose corresponding to 29.1g/l cell mass. Volumetric oxygen transfer coefficient (K(L)a) increased with the increasing of agitation rate.     

Hyperproduction of cordycepin by two-stage dissolved oxygen control in submerged cultivation of medicinal mushroom Cordyceps militaris in bioreactors

Effect of oxygen supply on cordycepin production was investigated in submerged cultivation of Cordyceps militaris, a famous traditional Chinese medicinal mushroom, in a 5-L turbine-agitated bioreactor (TAB). Initial volumetric oxygen transfer coefficient (kLa) within the range of 11.5-113.8 h(-1) had significant influence on cordycepin production. The highest cordycepin concentration of 167.5 mg/L was obtained at an initial kLa value of 54.5 h(-1), where a moderate dissolved oxygen (DO) pattern was observed throughout cultivation. The possible correlation between cordycepin production and DO level was explored by DO control experiments, and the results showed that DO within the range of 10-80% of air saturation greatly affected the cultivation process. To obtain a high specific cordycepin formation rate (rho) throughout cultivation, a two-stage DO control strategy was developed based on the analysis of the relationship of rho and DO. That is, DO was controlled at 60% from the beginning of cultivation and then shifted to a lower control level of 30% when rho started to decrease. As a result, a high cordycepin production of 201.1 mg/L and a high productivity of 15.5 mg/(L.d) were achieved, which was enhanced by about 15% and 30% compared to the highest titers obtained in conventional DO control experiments, respectively. The proposed DO control strategy was also applied to a recently developed 5-L centrifugal impeller bioreactor (CIB) with cordycepin production and productivity titers of 188.3 mg/L and 14.5 mg/(L.d). Furthermore, the scale-up of the two-stage DO control process from 5-L CIB to 30-L CIB was successfully demonstrated. The work is useful for the efficient large-scale production of bioactive metabolites by mushroom cultures.     

Overexpression of a modified protein from amaranth seed in Escherichia coli and effect of environmental conditions on the protein expression

Amaranth seeds are considered as an excellent complementary source of food protein due to their balanced amino acid composition. Amarantin acidic subunit has the potential as a functional and nutraceutical protein, and it is structurally a good candidate for modification. The aim of this work was to improve its functionality, then the primary structure was modified into the third variable region of 11S globulins, by inserting antihypertensive peptides: four Val-Tyr in tandem and Arg-Ile-Pro-Pro in the C-terminal region. Modified protein was expressed in Escherichia coli Origami (DE3) and was purified. The culture conditions, including the culture media, temperature, agitation speed and air flow were tested in order to obtain an increased expression levels of the modified protein. A 2(3) factorial design was used for evaluate the effect of environmental conditions on modified protein production. The results indicated that the yield of modified protein could be increased by up 3-fold in bioreactor as compared with flask. In addition, the temperature, the agitation speed and the oxygen were significant factors on the expression of the antihypertensive protein. The maximum production was 99 mg protein-L(-1). The hydrolyzed protein showed a high inhibitory activity of the angiotensin converting enzyme (IC50=0.047 mg mL(-1)).     

Production of a recombinantly expressed laminin fragment by HEK293-EBNA cells cultured in suspension in a dialysis-based bioreactor

Laminin 5 is a multifunctional extracellular matrix protein, which supports epithelial cell adhesion through multiple cell binding sites. For elaborate studies, a 35 kDa fragment localized at the C-terminal extremity of the molecule, the LG4/5 fragment was recombinantly expressed in mammalian HEK293-EBNA cells. As the production of the LG4/5 fragment by adherent cell monolayers was very low (<1 microg/ml), we used the commercially available small scale bioreactor system miniPERM. The HEK293-EBNA transfectants were adapted to grow in suspension in defined medium containing low level of fetal calf serum and produced the recombinant LG4/5 protein with quality consistent with that produced in conventional static cell culture conditions. Cells grew without forming aggregates in the bioreactor and the resulting HEK293-EBNA-LG4/5 cell line was suitable for unlimited passages in the bioreactor. 2.5x10(5) cells/ml were cultured for 25 days to reach the maximal cell density of 1.6x10(7) cells/ml. The quantification of protein synthesis revealed that the highest level of 2.4 mg of recombinant LG4/5 protein was harvested when 10(7) transfected cells/ml were injected in the bioreactor and allowed to grow for 2 days. The mean daily recombinant LG4/5 fragment product yield of 1.2 mg of protein per minifermenter shows that cultivation of HEK293-EBNA transfectants in suspension is highly convenient for the production of recombinant laminin fragments.     

Increased Hepatitis B surface antigen production by recombinant <Emphasis Type="BoldItalic">Aspergillus niger</Emphasis> through the optimization of agitation and dissolved oxygen concentration

The capacity of the filamentous fungi Aspergillus niger to produce and assemble complex immunogenic viral proteins into virus-like particles (VLPs) in batch culture was enhanced by optimizing the bioprocessing parameters, agitation intensity and dissolved oxygen (dO₂) concentration. Response surface methodology (RSM) and a two-factor-two-level central composite rotatable design (CCRD) were employed to evaluate the interactive response pattern between parameters and their optimum combination. The recombinant hepatitis B surface antigen (HBsAg) was used as a model VLP system to determine the effect of these parameters on biomass yield, fungal morphology, HBsAg production and bioreactor kinetics. The response surface model predicted optimum cultivation conditions at an agitation of rate of 100 rpm and a dO₂ concentration of 25%, obtaining highest intracellular membrane-associated HBsAg levels of . HBsAg production levels were increased tenfold compared to yields obtained in shake flask cultivation. Although hepatitis B VLPs mostly accumulated intracellularly, optimal bioreactor conditions resulted in significant HBsAg release in culture supernatant. These results compare favourably with other recombinant VLP systems in batch culture, and therefore, indicate a substantial potential for further engineering of the A. niger production system for the high level of intracellular and extracellular VLP production.     

Culture media optimization for Chinese hamster ovary cell growth and expression of recombinant varicella-zoster virus glycoprotein E

Herpes zoster (HZ) is caused by reactivation of varicella-zoster virus (VZV) latent in the sensory ganglia and causes severe pain, often leading to postherpetic neuralgia (PHN). Two prophylactic vaccines against HZ are currently licensed for human use, a live attenuated vaccine and a subunit vaccine containing recombinant VZV glycoprotein E (gE) as antigen. The latter has superior protective efficacy against HZ and PHN. During HZ subunit vaccine development, we obtained Chinese hamster ovary (CHO) cell clones expressing VZV gE. This study was performed to optimize culture media conditions for CHO cell growth and gE production. Using a high-throughput culture system, three CHO cell clones were cultured in microtiter plates containing 24 different basal media, and three basal media were selected. The clone with the highest gE expression was fed-batch cultured in each of the three basal media in combination with 13 different feed media. A pair of media, BalanCD CHO Growth A and EX-CELL Advanced CHO Feed 1, with the highest productivity was selected for gE production. Scale-up fed-batch cultures of the selected clone cultured in a wave bag bioreactor containing the optimized media yielded 2440 mg gE protein/L culture, a 11.5-fold increase compared to original culture conditions (batch culture in CD OptiCHO medium). The optimized media condition is used to produce VZV gE antigen for an HZ subunit vaccine, which is under phase I clinical trial. This study would provide valuable insights on culture media optimization for CHO cells expressing a recombinant vaccine antigen.

     

Enhanced benzaldehyde formation by a monokaryotic strain of Pycnoporus cinnabarinus using a selective solid adsorbent in the culture medium.

A monokaryotic strain of the white-rot fungus Pycnoporus cinnabarinus was shown to produce, in a 2-L bioreactor culture, 100 mg.L-1 benzaldehyde (bitter almond aroma) from L-phenylalanine with a productivity of 33 mg.L-1.day-1. The addition of HP20 resin, a styrene divinylbenzene copolymer highly selective for benzaldehyde, enabled an eightfold increase in the production of benzaldehyde and a twofold increase in productivity. In the presence of HP20 resin, the production of 790 mg.L-1 benzaldehyde was concomitant with the synthesis of cinnamic acid derivatives of high organoleptic notes such as cinnamaldehyde, cinnamyl alcohol, and methyl cinnamate.     

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.     

Dynamics of recombinant protein production by mammalian cells in immobilized perfusion culture

In spite of the generally stable nature of immobilized perfusion culture, its profile of target protein production frequently shows variations. This might be explained by the drift in the metabolism of cultured cells. To address this issue, we performed a set of four Opticell bioreactor cultures producing recombinant anticogulant protein PCGFX. All the cultures lasted 40-50 days with the oxygen consumption rate (OCR) mostly around 10 μmol min⁻¹; nevertheless, glucose and lactate metabolism was fluctuated with a parallel fluctuation in the recombinant protein productivity (RPP). The mean productivity of recombinant PCGFX was determined to be about 1.0 mg day⁻¹ for all the cultures. The statistical analysis revealed a significant correlation between the lactate production rate (LPR) and RPP in two cultures. A significant correlation was further found between average OCR and RPP in another culture where OCR was exceptionally lowered under serum-free conditions. No parameter significantly correlated with RPP in the remaining one culture; thus, the overt drift of RPP resulted, at least partly, from that of the cell metabolic activity and the present data should be helpful to explore a strategy for maximizing productivity.     

人促血小板生成素在转基因小鼠乳腺中定位表达的研究(英文)

通过转基因动物乳腺生物反应器大规模生产药用蛋白质已成为现代生物技术新的生长点之一。为研制表达人促血小板生成素的哺乳动物生物反应器的转基因小鼠模型,本论文以小鼠乳清酸蛋白 (mWAP) 基因5挾说骺厍团-s1-酪蛋白基因3挾说骺厍魑鹘谠菇擞糜诒泶锶舜傺“迳伤氐娜橄僮橹匾煨员泶镌靥錺WAPTPO(Fig.1)。通过常规显微注射的方法把mWAP启动子指导的hTPO表达载体导入小鼠受精卵,获得出生小鼠16只。经PCR检测,有6只为转基因阳性(Fig.2)。G0代小鼠中转基因整合率为37.5% (6/16),用ELISA方法在G0代转基因雌鼠的乳汁中检测了促血小板生成素的表达,表达量在0.8 mg/mL以上(Table 1)。这些结果表明我们已建立了乳腺表达hTPO 的转基因小鼠模型,为以后大型家畜乳腺生物反应器的研制提供了科学依据。     

Effect of submerged culture conditions on exopolysaccharides production by Armillaria luteo-virens Sacc QH and kinetic modeling

This work aimed to develop the submerged cultivation conditions for improved exopolysaccharides (EPS) production by Armillaria luteo-virens Sacc. The effects of culture temperature, aeration rate, inoculum level, initial pH, and additives on EPS formation and mycelial growth are investigated. The aeration rate, initial pH, and inoculum level significantly affected EPS production under the submerged cultivation. The developed conditions were as follows: cultivation temperature 23 °C, initial pH 5.0, aeration rate 0.5 vvm, 0.5% Tween 80, inoculum level 5% (v/v), and shaking speed 120 r/min. Under the developed conditions, the highest EPS production was 13.01 g/L at 5 days culture time. EPS production was examined in a 5 L bioreactor, and an unstructured kinetic model for EPS formation was well developed. The verified investigations in the large-scale cultivation system showed that the developed models are able to predict the submerged cultivation process of EPS formation. Current results revealed that the submerged cultivation conditions can be utilized to control EPS production, and the unstructured models developed are suitable for explaining EPS production by A. luteo-virens Sacc QH in a large-scale cultivation bioreactor.     

Application of a two-dimensional disposable rocking bioreactor to bacterial cultivation for recombinant protein production

Disposable rocking bioreactors (RBs) are widely employed for cultivation of recombinant mammalian and insect cell lines, although the perception of inadequate mass transfer has prevented their application to bioprocesses based on microbial platforms. In this study, one-dimensional (1D) and two-dimensional (2D) RBs were assessed and compared with the conventional stirred tank reactor (STR) for recombinant therapeutic protein production in Escherichia coli. The comparison involved: (1) physical characterization of oxygen mass transfer efficiency and mixing intensity, (2) growth characteristics in batch cultivation, and (3) culture performance for the production of recombinant protein. Our results show that oxygen mass transfer was comparable between the 1D RB and STR at low working volume (WV), declining linearly with increasing WV, and was highest in the 2D RB for all tested WVs with the maximum mass transfer coefficient (k_La) at 3 L WV. Well mixing behavior was observed in all three systems for water and aqueous carboxymethylcellulose (CMC) solutions. Batch growth characteristics were similar in all bioreactor systems, although metabolite accumulation was significant in the 1D RB. Culture performance for the production of recombinant GST-hCD83ext (glutathione S-transferase-hCD83ext fusion protein) was similar in terms of soluble protein yield and inclusion body formation for all bioreactor systems.     

High level expression of human endostatin in Pichia pastoris using a synthetic gene construct

Endostatin, a 20-kDa C-terminal fragment derived from type XVIII collagen, is a potent angiogenesis inhibitor and an antitumor factor. To improve the production of recombinant human endostatin on increasing demand in clinical practice, we constructed an artificial gene encoding its mature peptide sequence in human collagen XVIII. The synthetic gene consisted of 20 codons in preference in methylotropic yeast—Pichia pastoris and was cloned into expression vector pPICZαA; and the recombinant protein was expressed in P. pastoris strain SMD1168 and purified to near homogeneity using heparin affinity chromatography. The amount of expressed recombinant protein in cultural media using described strategy was 80 mg/l in shake flask cultivation and 435 mg/l in high-density bioreactor fermentation. Methylthiazolium assay demonstrated that human endostatin expressed in P. pastoris using artificial synthetic gene of preference in P. pastoris was able to inhibit the acidic fibroblast growth factor-induced proliferation of endothelial cells in vitro.     

High bioreactor production and emulsifying activity of an unusual exopolymer by Chromohalobacter canadensis 28

Unusual composition of an exopolymer (EP) from an obligate halophilic bacterium Chromohalobacter canadensis 28 has triggered an interest in development of an effective bioreactor process for its production. Its synthesis was investigated in 2‐L bioreactor at agitation speeds at interval 600‐1000 rpm, at a constant air flow rate of 0.5 vvm; aeration rates of 0.5, 1.0, and 1.5 vvm were tested at constant agitation rate of 900 rpm. EP production was affected by both, agitation and aeration. As a result twofold increase of EP yield was observed and additionally increased up to 3.08 mg/mL in a presence of surfactants. For effective scale‐up of bioreactors mass transfer parameters were estimated and lowest values of K_La obtained for the highest productivity fermentation was established. Emulsification activity of EP exceeded that of trade hydrocolloids xanthan, guar gum, and cellulose. A good synergism between EP and commercial cellulose proved its potential exploration as an enhancer of emulsifying properties of trade emulsions. A pronounced lipophilic effect of EP was established toward olive oil and liquid paraffin. Cultivation of human keratinocyte cells (HaCaT) with crude EP and purified γ‐polyglutamic acid (PGA) showed higher viability than control group.     

Modeling and optimization of poly(3hydroxybutyrate-co-3hydroxyvalerate) production from cane molasses by Azohydromonas lata MTCC 2311 in a stirred-tank reactor: effect of agitation and aeration regimes

The effects of agitation and aeration rates on copolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] production by Azohydromonas lata MTCC 2311 using cane molasses supplemented with propionic acid in a bioreactor were investigated. The experiments were conducted in a three-level factorial design by varying the impeller (150-500 rev min(-1)) and aeration (0.5-1.5 vvm) rates. Further, the data were fitted to mathematical models [quadratic polynomial equation and artificial neural network (ANN)] and process variables were optimized by genetic algorithm-coupled models. ANN and hybrid ANN-GA were found superior for modeling and optimization of process variables, respectively. The maximum copolymer concentration of 7.45 g l(-1) with 21.50 mol% of 3HV was predicted at process variables: agitation speed, 287 rev min(-1); and aeration rate, 0.85 vvm, which upon validation gave 7.20 g l(-1) of P(3HB-co-3HV) with 21 mol% of 3HV with the prediction error (%) of 3.38 and 2.32, respectively. Agitation speed established a relative high importance of 72.19% than of aeration rate (27.80%) for copolymer accumulation. The volumetric gas-liquid mass transfer coefficient (k (L) a) was strongly affected by agitation and aeration rates. The highest P(3HB-co-3HV) productivity of 0.163 g l(-1) h(-1) was achieved at 0.17 s(-1) of k (L) a value. During the early phase of copolymer production process, 3HB monomers were accumulated, which were shifted to 3HV units (9-21%) during the cultivation period of 24-42 h. The enhancement of 7.5 and 34% were reported for P(3HB-co-3HV) production and 3HV content, respectively, by hybrid ANN-GA paradigm, which revealed the significant utilization of cane molasses for improved copolymer production.     

Inactivation of Bacteriophages by Thiol Reducing Agents

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 °C during the protein production phase increased production of the protein two-fold compared to 37 °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 μg EGFP/10⁶ infected cells, or 27 mg EGFP per liter.     

Development of a fed-batch process for the production of the cytochrome P450 monooxygenase CYP102A1 from Bacillus megaterium in E. coli

A fed-batch process utilizing a pET-based expression system (pET28a+ derivative) and E. coli BL21(DE3) as production strain for the heterologous expression of recombinant cytochrome P450 monooxygenase CYP102A1 from Bacillus megaterium was developed. In a first step the expression was optimized during a series of flask experiments testing several parameters for their influence on the expression level, activity and solubility of the recombinant protein. The optimal process parameters found in the flask experiments were transferred to a cultivation process in a 5l (operating volume) bioreactor with a special focus on the feeding strategy and the aeration during expression. Glycerol feeding proved to be superior over glucose as carbon source since the formation of larger amounts of acetate was prevented. Expression levels exceeding 12,500nmoll(-1), corresponding to approximately 1.5gl(-1) of product in culture medium ( approximately 11% of CDW) could be demonstrated. The P450 enzyme showed high activity and high solubility. The findings now can be transferred to other enzyme variants and different P450 monooxygenases to increase production of recombinant proteins.