Production of recombinant herpes simplex virus protease in 10-L stirred vessels using a baculovirus–insect cell expression system

A gene expression system using recombinant Autographa californica nuclear polyhedrosis virus (baculovirus) and Sf-9 cells has been scaled up to the 10-L tank level and shown to be capable of producing herpes simplex virus (HSV) protease in serum-free media. High densities of Spodoptera frugiperda (Sf-9) cells were achieved by modifying two 10-L Biolafitte fermenters specifically for insect cell growth. The existing Rushton impellers were replaced by marine impellers to reduce shear and the aeration system was modified to allow external addition of air/O₂ mixtures at low flow rates through either the sparge line or into the head space of the fermenter. To inoculate the tanks, Sf-9 cells were adapted to grow to high cell densities (6–10 × 10⁶ cells ml⁻¹) in shake flasks in serum-free media. With these procedures, cell densities of 5 × 10⁶ cells ml⁻¹ were routinely achieved in the 10-L tanks. These cells were readily infected with recombinant baculovirus expressing the 247-amino acid catalytic domain of the HSV-1 strain 17 protease UL26 gene as a glutathione-S-transferase (GST) fusion protein (GST-247). Three days after infection at a multiplicity of infection (MOI) of 3 pfu cell⁻¹, the GST-247 fusion protein was purified from a cytoplasmic lysate by Glutathione Sepharose 4-B affinity chromatography with reproducible yields of 11–38 mg L⁻¹ of recombinant protein and ≥ 90% purity. Maximum production of this protein was observed at a cell density of 5.0 × 10⁶ cells ml⁻¹. Received 09 December 1996/ Accepted in revised form 13 April 1997     

Large scale transient 5-HT3 receptor production with the Semliki Forest Virus Expression System

The expression of recombinant proteins with the Semliki Forest Virus (SFV) system has been scaled up to bioreactor scale. As a model protein for this study the human 5-HT₃ receptor was chosen. The gene for the receptor was subcloned into the SFV expression plasmid pSFV1. Virus production by in vivo packaging and production of the recombinant protein was scaled up, the latter to a reactor volume of 11.5 l. A Vibromix^TM agitation system was chosen to overcome aggregation problems of BHK cells in suspension. In the process, cells were first grown to a density of 10⁶ cells/ml, the medium was then exchanged with fresh medium and the culture was infected with the recombinant virus at an estimated multiplicity of infection of 30. 24 h post infection we measured an expression level of 3 million functional 5-HT₃ receptors per cell. For harvesting, the cells were pelleted by centrifugation. The receptor protein was purified in a single step (Hovius et al., 1998) by exploiting the hexa-His tag at minimal protein loss (51% yield). Experiments to optimise expression resulted in yields up to 8 million receptors per cell, when the pH of a suspension culture was controlled at pH 7.3. Rapid virus generation and protein production, high protein yields as well as successful large scale application have made the SFV expression system attractive to produce large quantities of recombinant protein in a very short time. After optimisation of the expression conditions (in particular by setting the pH at 7.3), yields were increased twofold.     

The indirect effects of multiplicity of infection on baculovirus expressed proteins in insect cells: secreted and non-secreted products

The baculovirus expression vector system was employed to produce human apolipoprotein E and β-galactosidase in order to study the effect of multiplicity of infection on secreted and non-secreted recombinant protein production. Prior knowledge of the influence of other cell culture and infection parameters, such as the cell density at time of infection and the time of harvest, allowed determination of the direct and indirect influences of multiplicity of infection on recombinant protein synthesis and degradation in insect cells. Under non-limited, controlled conditions, the direct effect of multiplicity of infection (10⁻¹−10 pfu/cell) on specific recombinant product yields of non-secreted β-galactosidase was found to be insignificant. Instead, the observed increased in accumulated product was directly correlated to the total number of infected cells during the production period and therefore ultimately dependent on an adequate supply of nutrients. Only the timing of recombinant virus and protein production was influenced by, and dependent on the multiplicity of infection. Evidence is presented in this study that indicates the extremely limited predictability of post-infection cell growth at very low multiplicities of infection of less than 0.1 pfu/cell. Due to the inaccuracy of the current virus quantification techniques, combined with the sensitivity of post-infection cell growth at low MOI, the possibility of excessive post-infection cell growth and subsequent nutrient limitation was found to be significantly increased. Finally, as an example, the degree of product stability and cellular and viral protein contamination at low multiplicity of infection is investigated for a secreted recombinant form of human apolipoprotein E. Comparison of human apolipoprotein E production and secretion at multiplicities of infection of 10⁻⁴−10 pfu/cell revealed increased product degradation and contamination with intracellular proteins at low multiplicities of infection. This revised version was published online in July 2006 with corrections to the Cover Date.     

Aujeszky’s disease virus production in disposable bioreactor

A novel, disposable-bag bioreactor system that uses wave action for mixing and transferring oxygen was evaluated for BHK 21 C13 cell line growth and Aujeszky’s disease virus (ADV) production. Growth kinetics of BHK 21 C13 cells in the wave bioreactor during 3-day period were determined. At the end of the 3-day culture period and cell density of 1.82 × 10⁶ cells ml^-1, the reactor was inoculated with 9 ml of gE^- Bartha K-61 strain ADV suspension (10^5.9 TCID₅₀) with multiplicity of infection (MOI) of 0.01. After a 144 h incubation period, 400 ml of ADV harvest was obtained with titre of 10^7.0 TCID₅₀ ml⁻¹, which corresponds to 40,000 doses of vaccine against AD. In conclusion, the results obtained with the wave bioreactor using BHK 21 C13 cells showed that this system can be considered as suitable for ADV or BHK 21 C13 cell biomass production.     

Heterologous expression and characterization of a recombinant thermostable alkylsulfatase (<Emphasis Type="Italic">sdsAP</Emphasis>)

A novel alkylsulfatase gene, sdsAP, was cloned from a newly isolated bacterium Pseudomonas sp. S9. It encoded a protein of 675 amino acids with a calculated molecular mass of 74.9 kDa. The protein contained a typical N-terminal signal peptide of 41 amino acid residues, followed by a metallo-β-lactamase like domain at the N-terminus and a SCP-2-like domain at the C-terminus. This domain organization mode suggested that it belonged to the type III sulfatase. The mature alkylsulfatase was overexpressed in Escherichia coli. The optimal temperature and pH of the recombinant SdsAP were 70°C and 9.0, respectively. Notably, at optimal conditions, the purified recombinant SdsAP had a high specific activity of 23.25 μmol min⁻¹ mg⁻¹, a K _{m (app)} of 264.3 μmol, and a V _{max (app)} of 33.8 μmol min⁻¹ mg⁻¹ for SDS. Additionally, it still retained more than 90% activity after incubation at 65°C for 1 h, which was much different from other alkylsulfatases reported. The recombinant enzyme hydrolyzed the primary alkyl sulfate such as sodium octyl sulfate and sodium dodecyl sulfate (SDS). It was a Zn²⁺-containing and Ca²⁺ activated alkylsulfatase. This is the first report to explore the various characteristics of the heterologous recombinant alkylsulfatase in details. These favorable properties could make SdsAP attractive to be useful in the degradation of SDS-containing waste.     

Effects of Calmodulin and Ca<Superscript>2+</Superscript> Channel Blockers on ω-conotoxin GVI A Binding to Crude Membranes from α<Subscript>1B</Subscript> Subunit (Ca<Subscript>v</Subscript>2.2) Expressed BHK Cells and Mice Brain Lacking the α<Subscript>1B</Subscript> Subunits

Characteristics for the specific binding of ¹²⁵I-ω-CTX GVIA and ¹²⁵I-ω-CTX MVIIC to crude membranes from BHKN101 cells expressing the α_1B subunits of Ca_v2.2 channels and from mice brain lacking the α_1B subunits of Ca_v2.2 channels, particularly, the effects of CaM and various Ca²⁺ channel blockers on these specific bindings were investigated. Specific binding of ¹²⁵I-ω-CTX GVIA to the crude membranes from BHKN101 cells was observed, but not from control BHK6 cells. ω-CTX GVIA, ω-CTX MVIIC and ω-CTX SVIB inhibited the specific binding of ¹²⁵I-ω-CTX GVIA to crude membranes from BHKN101 cells, and the IC₅₀ values for ω-CTXGVIA, ω-CTX MVIIC and ω-CTX SVIB were 0.07, 8.5 and 1.7 nM, respectively. However, ω-agatoxin IVA and calciseptine at concentrations of 10⁻⁹–10⁻⁶ M did not inhibit specific binding. Specific binding was also about 80% inhibited by 20 μg protein/ml CaM. The amount of ¹²⁵I-ω-CTX GVIA (30 pM) specifically bound to membranes from brain of knockout mice lacking α_1B subunits of Ca_v2.2 channels was about 30% of that to the crude membranes from brain of wild-type. On the other hand, specific binding of ¹²⁵I-ω-CTX MVIIC (200 pM) was observed on the crude membranes of both BHKN101 and control BHK6 cells. The specific binding of ¹²⁵I-ω-CTX MVIIC (200 pM) was not inhibited by ω-CTX GVIA and ω-CTX SVIB, and also ω-Aga IVA and calciseptine at concentrations of 10⁻⁹–10⁻⁷ M, although specific binding was almost completely dose dependently inhibited by non-radiolabeled ω-CTX MVIIC (IC₅₀ value was about 0.1 nM). 20 μg protein/ml CaM did not inhibit specific binding. Therefore, these results suggest that BHKN101 cells have a typical Ca_v2.2 channels which are also inhibited by CaM and have not specific binding sites for ω-CTX MVIIC, although ω-CTX MVIIC is a blocker for both Ca_v2.1 (α_1A; P/Q-type) and Ca_v2.2 channels.     

Two-stage continuous operation of recombinant Escherichia coli using the bacteriophage λ Q − vector

A two-stage continuous culture of Escherichia coli in combination with a bacteriophage λ system was performed in order to overcome the intrinsic plasmid instability that is frequently observed in recombinant fermentation. A phage λ vector with a Q ⁻ mutation was used to enhance the expression of the λ system. The optimal values of the important operational variables such as the substrate concentration, the dilution rate, and the mean residence time on the expression of the cloned gene were determined in both batch and continuous cultures. For all culturing modes, the full induction of the cloned gene was observed 4 h after the temperature shift. In the two stage continuous culture, the overproduction reached their maxima at D=0.25 h⁻¹ with 1.5 S ₀ of the medium supply. The maximum productivity of the total β-galactosidase was 16.3×10⁶ U l⁻¹ h⁻¹, which was approximately seven times higher than that in the single-copy lysogenic stage. The recombinant cells were stable in the lysogenic state for more than 260 h, while they were stable for 40 h in the lytic state. The instability that developed rapidly in the second tank is believed to be due to the accumulation of lysis proteins as a result of vector leakage during the operation.     

Kinetic studies of recombinant human interferon-gamma expression in continuous cultures of <Emphasis Type="Italic">E. coli</Emphasis>

A series of continuous cultures was performed to understand the product formation kinetics of recombinant human interferon gamma (rhIFN-γ) in Escherichia coli at different dilution rates ranging from 0.1 to 0.3 h⁻¹ in different media. A T7 promoter-based vector was used for expression of IFN-γ in E. coli BL21 (DE3) cells. The recombinant protein was produced as inclusion bodies, thus allowing a rapid buildup of rhIFN-γ inside the cell, with the specific product yield (Y _p/X ) reaching a maximum value of 182 mg g⁻¹ dry cell weight (DCW). In all the media tested, the specific product formation rate (q _p ) was found to be strongly correlated with the specific growth rate (μ), demonstrating the growth-associated nature of product formation. The q _p values show no significant decline with time postinduction, even though the recombinant protein has been over produced inside the cell. The maximum q _p level of 75.5 mg g⁻¹ h⁻¹ was achieved at the first hour of induction at the dilution rate of 0.3 h⁻¹. Also, this correlation between q _p and μ was not critically dependent on media composition, which would made it possible to grow cells in defined media in the growth phase and then push up the specific growth rate just before induction by pulse addition of glucose and yeast extract. This would ensure the twin objectives of high biomass and high specific productivities, leading to high volumetric product concentration.     

Physiological response of bovine subcommissural organ to endothelin 1 and bradykinin

Elevated glutamate levels have been reported in humans with diabetic retinopathy. Retinal Müller glial cells regulate glutamate levels via the GLAST transporter and system x_c ⁻ (cystine-glutamate exchanger). We have investigated whether transporter function and gene and/or protein expression are altered in mouse Müller cells cultured under conditions of hyperglycemia or oxidative stress (two factors implicated in diabetic retinopathy). Cells were subjected to hyperglycemic conditions (35 mM glucose) over an 8-day period or to oxidative stress conditions (induced by exposure to various concentrations of xanthine:xanthine oxidase) for 6 h. The Na⁺-dependent and –independent uptake of [³H] glutamate was assessed as a measure of GLAST and system x_c ⁻ function, respectively. Hyperglycemia did not alter the uptake of [³H] glutamate by GLAST or system x_c ⁻; neither gene nor protein expression decreased. Oxidative stress (70:14 or 100:20 μM xanthine:mU/ml xanthine oxidase) decreased GLAST activity by ~10% but increased system x_c ⁻ activity by 43% and 89%, respectively. Kinetic analysis showed an oxidative-stress-induced change in V_max, but not K_m. Oxidative stress caused a 2.4-fold increase in mRNA encoding xCT, the unique component of system x_c ⁻. Of the two isoforms of xCT (40 and 50 kDa), oxidative stress induced a 3.6-fold increase in the 40-kDa form localized to the plasma membrane. This is the first report of the differential expression and localization of xCT isoforms as caused by cellular stress. Increased system x_c ⁻ activity in Müller cells subjected to conditions associated with diabetic retinopathy may be beneficial, as this exchanger is important for the synthesis of the antioxidant glutathione. This work was supported by NIH R01 EY014560.     

Cell cycle phase dependent productivity of a recombinant Chinese hamster ovary cell line

A Chinese Hamster Ovary cell line, CHO1-15₅₀₀, producing recombinant human tissue type plasminogen activator (tPA) via the dihydrofolate reductase (DHFR) amplification system, was studied in batch culture. In this system both DHFR and tPA are under the control of the strong constitutive viral SV40 early promoter. Employing the cumulative viable cell-hour approach, the specific productivity of tPA had maxima in the lag (0.065 pg cell⁻¹ h⁻¹) and early decline (0.040 pg cell⁻¹ h⁻¹) population growth phases. The viable population was assigned into four subpopulations (G1, S, G2/M phase, and Apoptotic cells) using flow cytometric analysis. As expected, intracellular DHFR was maximally expressed during the S cell cycle phase. The production of tPA, however, was found to be a direct linear function of the G1 phase, with a subpopulation specific productivity of 0.080 pg c-h⁻¹. Productivity maxima in the lag and early decline corroborate the flow cytometric data, indicative that this recombinant tPA production occurs primarily in the G1 cell cycle phase, not the S phase. This suggests that endogenous regulatory mechanisms are important controlling influences on the production of recombinant tPA in this ovarian cell line. Productivity from recombinant cell lines cannot be inferred from either the plasmid construct or the host cell alone. Elucidation of the relationship between expression of recombinant protein and the cell cycle phases of the host cell is a major component of the characterization of the animal cell production system. This information facilitates rational process design, including operating mode, modelling and control, and medium formulation.     

Effect of amplification ofdhfr andlac Z genes on growth and β-galactosidase expression in suspension cultures of recombinant CHO cells

Studies were conducted to characterize the effect of gene amplification and foreign gene expression on recombinant CHO cell growth. Chinese hamster ovary (CHO) cells were transfected with an expression vector containing the gene for dihydrofolate reductase (dhfr) and the gene for human β-interferon (β-IFN) or thelac Z gene which codes for β-galactosidase (β-gal). The recombinant genes in these CHO cells were amplified stepwise by growth in 0, 10⁻⁷, and 10⁻⁶ M methotrexate (MTX), and the β-gal expressing cells were adapted to suspension culture. Flow cytometric methods (FCM) were used to measure the distribution of amplifieddhfr gene content and foreign β-gal gene expression in the cell populations. A biochemical assay for β-gal was also used. Beta-gal expression was found to increase with increasing gene amplification. The growth rate of recombinant CHO cells at 10⁻⁷ M MTX was found to be 20% lower than that of recombinant CHO cells in MTX-free medium, and the cell growth rate at 10⁻⁶ M MTX was 20% lower than that of recombinant CHO cells at 10⁻⁷ M MTX. There was no effect of 10⁻⁵ M MTX on the growth of CHO-DG44 (dhfr-) cells. The reduction of growth rate in recombinant CHO cells is therefore thought to be mainly due to the effect ofdhfr and foreign gene amplification and increased β-galactosidase expression.     

Citric acid production from sucrose using a recombinant strain of the yeast Yarrowia lipolytica

The yeast Yarrowia lipolytica is able to secrete high amounts of several organic acids under conditions of growth limitation and carbon source excess. Here we report the production of citric acid (CA) in a fed-batch cultivation process on sucrose using the recombinant Y. lipolytica strain H222-S4(p67ICL1) T5, harbouring the invertase encoding ScSUC2 gene of Saccharomyces cerevisiae under the inducible XPR2 promoter control and multiple ICL1 copies (10–15). The pH-dependent expression of invertase was low at pH 5.0 and was identified as limiting factor of the CA-production bioprocess. The invertase expression was sufficiently enhanced at pH 6.0–6.8 and resulted in production of 127–140 g l⁻¹ CA with a yield Y _CA of 0.75–0.82 g g⁻¹, whereas at pH 5.0, 87 g l ⁻¹ with a yield Y _CA of 0.51 gg⁻¹ were produced. The CA-productivity Q _CA increased from 0.40 g l ⁻¹ h⁻¹ at pH 5.0 up to 0.73 g l ⁻¹ h⁻¹ at pH 6.8. Accumulation of glucose and fructose at high invertase expression level at pH 6.8 indicated a limitation of CA production by sugar uptake. The strain H222-S4(p67ICL1) T5 also exhibited a gene–dose-dependent high isocitrate lyase expression resulting in strong reduction (<5%) of isocitric acid, a by-product during CA production.     

Expression of Ligand-Gated Ion Channels with the Semliki Forest Virus Expression System

Abstract

Two types of ligand-gated ion channels were expressed with the Semliki Forest virus (SFV) expression system.The cDNAs for mouse serotonin 5-HT₃ receptor and rat and human purinoreceptor P_2x subtypes were introduced into the pSFV1 vector. In vitro transcribed RNAs were coelectroporated with pSFV-Helper2 RNA into BHK cells, where in vivo packaging resulted in high titer SFV-5-HT₃ and SFV-P_2x virus stocks. Infection of BHK, CHO and RJN cells resulted in high-level expression of recombinant receptors. Saturation binding analysis indicated the presence of more than 3 × 10⁶ 5-HT3 receptors per cell. Binding studies on isolated membranes yielded from 10 to 60 pmol of either 5-HT₃ or P_2x receptor per mg protein. Functional responses to the P_2x receptors were demonstrated in SFV-infected CHO cells by Ca²⁺ mobilization or by ⁴⁵Ca²⁺ influx. High amplitude electrophysiological responses were also detected for both SFV-5-HT₃ and SFV-P_2x infected CHO cells in whole-cell patch clamp recordings. To facilitate the purification procedure of SFV-expressed recombinant receptors a histidine tag was introduced at the C-terminus of the 5-HT₃ receptor. This 5-HT₃His receptor showed high levels of expression, specific binding and high amplitude electrophysiological responses. For large scale expression the BHK cells were adapted to suspension culture and were efficiently infected in a 11.5 liter fermentor culture with SFV-5-HT3His resulting in high-level expression, 52 pmol receptor per mg protein corresponding to 3.2 × 10⁶ receptors per cell.     

Effects of temperature, and availability of nitrogen and phosphorus on the abundance of Anabaena and Microcystis in Lake Biwa, Japan: an experimental approach

Under optimal nutrient conditions, both Microcystis sp. and Anabaena sp. isolated from Lake Biwa grew optimally at 28–32°C but differed in maximal growth rates, phosphate uptake kinetics, maximal phosphorus quotas, and growth responses to nitrogen and phosphorus limitation. The maximal growth rates of Microcystis and Anabaena were 1.6 and 1.25 divisions day⁻¹, respectively. With phosphate and nitrate in the growth-limiting range, the growth of Microcystis was optimal at an N : P ratio of 100 : 1 (by weight) and declined at lower (nitrogen limitation) and higher (phosphorus limitation) ratios. In contrast, Anabaena growth rates did not change at N : P ratios from 1000 : 1 to 10 : 1. Starting with cells containing the maximal phosphorus quota, Microcystis growth in minus-phosphorus medium ceased in 7–9 days, compared with 12–13 days for Anabaena. The phosphate turnover time in cultures starved to their minimum cell quotas was 7.9 min for Microcystis and 0.6 min for Anabaena. Microcystis had a higher K _s (0.12 μg P l⁻¹ 10⁻⁶ cells) and lower V _max (9.63 μg P l⁻¹ h⁻¹ 10⁻⁶ cells), than Anabaena (K _s 0.02 μg P l⁻¹ h⁻¹ 10⁻⁶ cells; V _max 46.25 63 μg P l⁻¹ h⁻¹ 10⁻⁶ cells), suggesting that Microcystis would not be able to grow well in phosphorus-limited waters. We conclude that in spite of the higher growth rate under ideal conditions, Microcystis does not usually bloom in the North Basin because of low availability of phosphorus and nitrogen. Although Anabaena has an efficient phosphorus-uptake system, its main strategy for growth in low-phosphorus environments may depend on storage of phosphorus during periods of abundant phosphorus supply, which are rare in the North Basin. Received: July 31, 2000 / Accepted: October 18, 2000     

A Novel β-Agarase with High pH Stability from Marine Agarivorans sp. LQ48

A novel endo-type β-agarase gene, agaA, was cloned from a newly isolated marine bacterium, Agarivorans sp. LQ48. It encodes a protein of 457 amino acids with a calculated molecular mass of 51.2 kDa. The deduced protein contains a typical N-terminal signal peptide of 25 amino acid residues, followed by a catalytic module, which is homologous to that of glycoside hydrolase family 16. A sequence similar to a carbohydrate-binding module is found in the C-terminal region of the enzyme. The overall amino acid sequence shares a highest identity of 73% with the sequence of beta-agarase AgaB from Pseudoalteromonas sp. strain CY24. The mature agarase was highly expressed extracellularly in Escherichia coli. At pH 7.0 and 40°C, the purified recombinant AgaA had a high specific activity of 349.3 μmol min⁻¹ mg⁻¹, a K _m of 3.9 mg ml⁻¹, and a V _max of 909.1 μmol min⁻¹ mg⁻¹ for agarose. The recombinant enzyme hydrolyzed the β-1,4-glycosidic linkages of agarose, yielding neoagarotetraose and neoagarohexaose as the main products. Enzyme activity analysis revealed that the optimal temperature and pH of the recombinant AgaA were 40°C and 7.0, respectively. Notably, AgaA still retained more than 95% activity after incubation at pH 3.0–11.0 for 1 h, a characteristic much different from other agarases reported. It is the first agarase identified to have so wide a pH range stability. This favorable property could make AgaA to be attractive to the food, cosmetic, and medical industrial applications.     

Baculovirus production for gene therapy: the role of cell density,multiplicity of infection and medium exchange

One of the major concerns regarding the use of insect cells and baculovirus expression vectors for the production of recombinant proteins is the drop in production observed when infecting cultures at high cell densities; this work attempts to understand this so-called cell density effect in the scope of baculovirus production for gene therapy purposes. A Spodoptera frugiperda insect cell line (Sf-9) was cultured and infected in serum-free medium, and the patterns of production of a recombinant baculovirus expressing the green fluorescent protein (GFP) were analyzed at different cell concentrations at infection (CCIs) and multiplicities of infection (MOIs). The results confirm that a cell density effect on productivity occurs which is dependent on the MOI used, with a high MOI “delaying” the drop in production to higher cell densities. Medium replacement at the time of infection using a high MOI considerably improved baculovirus production, with the different production indicators, namely the titer, specific yield, amplification factor, and time of harvesting, increasing with cell concentration for the CCI range tested. Virus titers as high as 2.6 × 10¹⁰ IP.mL⁻¹ were obtained in cultures infected at 3.5 × 10⁶ cells.mL⁻¹, while the amplification factor was roughly 19 times higher than the highest value obtained without medium exchange.     

Optimization of culture on the overproduction of TRAIL in high-cell-density culture by recombinant Escherichia coli

Different nutrient-feeding cultures were carried out in producing recombinant protein of truncated tumor necrosis factor related apoptosis-inducing ligand (TRAIL) (114–281 amino acids of TRAIL) in Escherichia coli strain C600/pBV-TRAIL. The effects of preinduction specific growth rate, postinduction carbon source (glucose and glycerol), and feeding strategies were investigated. The higher preinduction specific growth rate (μ=0.22 h⁻¹) contributed to the increase in the TRAIL production, at which TRAIL was accumulated in bacterial cells as 7.2% of total cellular protein, corresponding to 1.99 g l⁻¹ in contrast with 5.1% (1.29 g l⁻¹) at preinduction specific growth rate (μ=0.1 h⁻¹) during high-cell-density culture. Glycerol was superior to glucose as the postinduction carbon source for TRAIL production. Under similar culture conditions, the final concentration of TRAIL was produced 1.59-fold more when glycerol was used as postinduction carbon source than when glucose was used. At the same time, the results showed that it is efficient to adopt the pH-stat feeding strategy at postinduction for the overproduction of TRAIL. The TRAIL production was increased up to 4.51 g l⁻¹, approximately 16.1% of total cellular protein. The mechanisms behind the preinduction specific growth rate effect on the expression level may be ascribed to the leakage secretion of acetate.     

Molecular cloning,sequence analysis,expression and characterization of the endochitinase gene from <Emphasis Type="Italic">Trichoderma</Emphasis> sp. in <Emphasis Type="Italic">Escherichia coli</Emphasis> BL21

The endochitinase DNA and cDNA from Trichoderma sp. were cloned, sequenced and expressed. The cloned DNA and cDNA sequences were 1,476 and 1,275 bp in length, respectively. There were three introns in DNA sequence in comparison with the cDNA sequence. The endochitinase protein contained three regions: the signal peptide, the prepro-region and the mature protein region. The gene fragment encoding the mature endochitinase was ligated into the expression vector pET-28a+, yielding pET-1. The plasmid pET-1 was transformed into the Escherichia coli BL21 (DE3). The clone bearing pET-1 was picked and cultured at 30°C for the expression of endochitinase. SDS-PAGE analysis showed that the endochitinase was expressed in the periplasmic space and the purified protein showed a single band. The activity of 70.2 U/mg was obtained from the cellular extract of the recombinant strain. The activity of endochitinase was 2.5-fold higher at 24 h than at 16 h in the periplasmic space. The optimal pH and temperature of the recombinant endochitinase were determined to be 7.0 and 35°C, respectively. It was relatively stable within the pH range of 5–8. Significant activity stimulation by 1 mM Mg²⁺ and 5 mM Fe²⁺ and inhibition by 5 mM Co²⁺ and 5 mM Hg²⁺ were observed. The kinetic constants K_m, V_max and K_cat for the hydrolysis of the colloidal chitin were 1.5 mM, 1.37 μmol min⁻¹ and 6.23 min⁻¹, respectively.     

High yield mixotrophic cultures of the marine microalga Tetraselmis suecica (Kylin) Butcher (Prasinophyceae)

The effects of three organic compounds were tested on one of the most used marine micro-algae in the aquaculture of molluscs and crustaceans, Tetraselmis suecica. Studies were made in axenic conditions with yeast extract, peptone and glucose added to the culture medium, each alone, in combinations of two or all together. Medium without any organic compound was used for the control. Cultures containing yeast extract grew best, reaching maximum cell density of 3.79 × 10⁶ and 3.84 × 10⁶ cells ml⁻¹. The organic carbon source affected the biochemical composition. The components most affected were the carbohydrates, with values between 6.5 pg cell⁻¹ in control cultures and 48.5 pg cell⁻¹ in glucose cultures. Protein content ranged between 27.5 pg cell⁻¹ in control cultures and 88.6 pg cell⁻¹ in yeast + glucose + peptone cultures. The lipid content changed little. Maximum protein yields were reached in cultures with yeast + glucose and with yeast - glucose - peptone, with values of 24.6 and 28.2 mg 1⁻¹ d⁻¹, respectively. These values are 22 and 25 times those in control cultures. A maximum carbohydrate yield of 7.9 mg carbohydrate per litre per day was obtained in yeast + glucose + peptone cultures, 27 times that in the control cultures. The maximum lipid yield was obtained with yeast + glucose + peptone and yeast + glucose. Maximum energy values were 308 kcal 1⁻ in yeast extract - glucose - peptone cultures and 279 kcal 1⁻¹ in yeast extract + glucose cultures. Gross energy values in control cultures were 24.5 kcal 1⁻¹, but peptone cultures presented the minimum energy value, 22 kcal 1⁻¹. The yeast extract: glucose ratio in the culture medium was optimized. A ratio 2:1 produced the best yields in cells, protein, carbohydrate and gross energy.     

Kinetic studies of constitutive human granulocyte-macrophage colony stimulating factor (hGM-CSF) expression in continuous culture of <Emphasis Type="Italic">Pichia pastoris</Emphasis>

Extracellular human granulocyte-macrophage colony stimulating factor (hGM-CSF) expression was studied under the control of the GAP promoter in recombinant Pichia pastoris in a series of continuous culture runs (dilution rates from 0.025 to 0.2 h⁻¹). The inlet feed concentration was also varied and the steady state biomass concentration increased proportionally demonstrating efficient substrate utilization and constancy of the biomass yield coefficient (Y_x/s) for a given dilution rate. The specific product formation rate (q_P) showed a strong correlation with dilution rates demonstrating growth associated product formation of hGM-CSF. The volumetric product concentration achieved at the highest feed concentration (4×) and a dilution rate of 0.2 h⁻¹ was 82 mg l⁻¹ which was 5-fold higher compared to the continuous culture run with 1× feed concentration at the lowest dilution rate thus translating to a 40 fold increase in the volumetric productivity. The specific product yield (Y_P/X) increased slightly from 2 to 2.5 mg g⁻¹, with increasing dilution rates, while it remained fairly invariant, for all feed concentrations demonstrating negligible product degradation or feed back inhibition. The robust nature of this expression system would make it easily amenable to scale up for industrial production.