Complete secretion of activable bovine prochymosin by genetically engineered L forms of Proteus mirabilis

To circumvent problems encountered in the synthesis of active chymosin in a number of bacteria and fungi, a recombinant DNA L-form expression system that directed the complete secretion of fully activable prochymosin into the extracellular culture medium was developed. The expression plasmid constructions involved the in-frame fusion of prochymosin cDNA minus codons 1 to 4 to streptococcal pyrogenic exotoxin type A gene (speA') sequences, including the speA promoter, ribosomal binding site, and signal sequence and five codons of mature SpeA. Secretion of fusion prochymosin enzymatically and immunologically indistinguishable from bovine prochymosin was achieved after transformation of two stable protoplast type L-form strains derived from Proteus mirabilis. The secreted proenzyme was converted by autocatalytic processing to chymosin showing milk-clotting activity. In controlled laboratory fermentation processes, a maximum specific rate of activable prochymosin synthesis of 0.57 x 10(-3)/h was determined from the time courses of biomass dry weight and product formation. Yields as high as 40 +/- 10 micrograms/ml were obtained in the cell-free culture fluid of strain L99 carrying a naturally altered expression plasmid of increased segregational stability. The expression-secretion system described may be generally useful for production of recombinant mammalian proteins synthesized intracellularly as aberrantly folded insoluble aggregates.     

Complete secretion of activable bovine prochymosin by genetically engineered L forms of Proteus mirabilis.

To circumvent problems encountered in the synthesis of active chymosin in a number of bacteria and fungi, a recombinant DNA L-form expression system that directed the complete secretion of fully activable prochymosin into the extracellular culture medium was developed. The expression plasmid constructions involved the in-frame fusion of prochymosin cDNA minus codons 1 to 4 to streptococcal pyrogenic exotoxin type A gene (speA') sequences, including the speA promoter, ribosomal binding site, and signal sequence and five codons of mature SpeA. Secretion of fusion prochymosin enzymatically and immunologically indistinguishable from bovine prochymosin was achieved after transformation of two stable protoplast type L-form strains derived from Proteus mirabilis. The secreted proenzyme was converted by autocatalytic processing to chymosin showing milk-clotting activity. In controlled laboratory fermentation processes, a maximum specific rate of activable prochymosin synthesis of 0.57 x 10(-3)/h was determined from the time courses of biomass dry weight and product formation. Yields as high as 40 +/- 10 micrograms/ml were obtained in the cell-free culture fluid of strain L99 carrying a naturally altered expression plasmid of increased segregational stability. The expression-secretion system described may be generally useful for production of recombinant mammalian proteins synthesized intracellularly as aberrantly folded insoluble aggregates.     

Efficient use of lactose for the lac promotercontrolled overexpression of the main antigenic protein of the foot and mouth disease virus in Escherichia coli under fed-batch fermentation conditions

Abstract: Derivatives of the lac promoter (tac, pac, rac) belong to the strongest bacterial promoters which are frequently used for the induced overexpression of foreign genes in Escherichia coli . However, their use in fermentation processes is strongly restricted because of the high cost of the inducer iso-propyl-β-D-thiogalactopyranoside (IPTG). The aim of this work was to investigate the possibility of using lac-derived promoters in high cell density processes resulting in a high yield of the induced recombinant protein if glucose is the main carbon and energy source. Lactose is tested as inducer of the main antigenic coat protein (VP1) of the foot and mouth disease (FMD) virus in a T7-RNA polymerase expression system. It was shown that lactose is able to induce the expression of the recombinant gene to an amount of the VP1 protein corresponding to 20% of the total cell protein.     

Examination of calf prochymosin accumulation in Escherichia coli: disulphide linkages are a structural component of prochymosin-containing inclusion bodies.

Recent reports have shown that synthesis of certain recombinant proteins in Escherichia coli results in the production of intracellular inclusion bodies. These studies have not analyzed the structure of the inclusion body especially regarding the intermolecular forces holding it together. We have examined structural aspects of inclusion bodies made in E. coli as a result of high level expression of the eukaryotic protein, calf prochymosin. Prochymosin is a monomeric protein containing three disulfide bridges. It was expressed at up to 20% of cell protein from a plasmid containing the E. coli tryptophan promoter, operator and ribosome binding site. Proteins in the inclusion bodies were analysed by Western blotting of SDS-polyacrylamide gels. When experiments were done using conditions which preserved the in vitro state of thiol groups, inclusions were shown to be composed of multimers of prochymosin molecules which were interlinked partly by disulfide bonds. The inclusion bodies also contained a high concentration of reduced prochymosin. The presence of intermolecular disulfides probably contributes to the difficulty of solubilizing recombinant prochymosin during its purification from E. coli.     

Effects of temperature and novobiocin on the expression of calf prochymosin gene and on plasmid copy number in recombinantEscherichia coli

Escherichia coli strain HB101 harboring an expression plasmid bearing calf prochymosin gene under the control of thetac promoter was grown in the presence of IPTG with or without novobiocin at 28 and 40 °C, respectively. The differential rates of synthesis of prochymosin inclusion, and, for comparison, of β-lactamase and β-galactosidase, as well as plasmid copy number, were determined during the first hours of steady state growth. At 28 °C the induced expression of prochymosin gene was almost blocked. Addition of novobiocin did not alleviate this effect. In fact, it strengthtened it, and we conclude that both these additive inhibitory effects are a consequence of the decrease in negative superhelical tension of plasmid DNA to an insufficient level. At 40 °C the differential rate of prochymosin synthesis was markedly enhanced. Since the copy number of the expression plasmid increased approximately to the same extent, we conclude that an increase in gene dose is the cause. The stimulation of cloned heterologous gene expression at 40 °C and inhibition at 28 °C may be conveniently used in biotechnological-scale cultivations of some recombinant bacteria.     

Effects of plasmid amplification and recombinant gene expression on the growth kinetics of recombinant E. coli

An experimental study was undertaken to identify and quantitate the effects of plasmid amplification and recombinant gene expression on Escherichia coli growth kinetics. Identification of these effects was possible because recombinant gene expression and plasmid copy number were controlled by different mechanisms on plasmid pVH106/172. Recombinant gene expression of the lactose operon structural genes was under the control of the lac promoter and was activated by the addition of the chemicals, IPTG and cyclic AMP, to the fermentation medium. Plasmid content was amplified in a separate fermentation by increasing culture temperature since the plasmid replicon was temperature-sensitive. A final fermentation was performed in which both plasmid content and recombinant gene expression were induced simultaneously by adding chemicals and raising the culture temperature. Recombinant growth rates were found to be reduced by the expression of high levels of recombinant lac proteins in the chemical induction experiments and by the amplification of plasmid levels in the temperature induction experiment. High expression of recombinant lac proteins following chemical induction was accompanied by a loss in recombinant cell viability. In the plasmid amplification experiment, the recombinant cells did not lose viability but the recombinant product yields were much lower than those achieved in the chemical induction experiments. Combining temperature and chemical induction increased the recombinant product yield by a factor of 4400 but also lowered cellular growth rates by 70%.     

Functional expression of human glucose-6-phosphate dehydrogenase in Escherichia coli

The complete coding sequence for human glucose-6-phosphate-dehydrogenase (G6PD) was inserted downstream from the tac promoter of a plasmid, pJF118EH, which also carries the lacIq repressor gene. When Escherichia coli strains (that are unable to grow on glucose due to the absence of functional zwf (G6PD-) and pgi genes) were transformed with this plasmid (pAC1), they were able to grow on glucose as sole carbon source. The rate of growth on glucose was faster in the presence of the inducer of the tac promoter, isopropyl-beta-D-thiogalactopyranoside (IPTG). Extracts of the transformed cells contained a G6PD activity that was not detectable in the parental strains and that was inducible by IPTG. The G6PD activities from normal E. coli and from pAC1-transformed cells comigrated with human G6PD when subjected to electrophoresis on agarose gels. However, when denatured, the G6PD produced by pAC1 was, like the human enzyme, distinguishable from the E. coli-encoded enzyme on the basis of its immunoreactivity with antibody specific for human G6PD. Therefore, human G6PD can be expressed in E. coli and can function to complement the bacterial enzyme deficiency.     

Investigation of the instability of plasmids directing the expression of Met-prochymosin in Escherichia coli

The causes of the instability of a multicopy plasmid, pCT70, which directs the expression of calf prochymosin in Escherichia coli, were investigated. Plasmid pAT153 and its derivative, pCT54, were stable for more than 90 generations in continuous culture with glucose limitation. The multicopy plasmid pCT66, which expressed very low levels of prochymosin due to poor translational efficiency, and low copy number plasmids which efficiently expressed the prochymosin gene, were also stable. These results indicated that high level translation of the recombinant gene was the cause of the instability of pCT70. The maximum specific growth rate of E. coli(pCT70) was reduced by 30% compared with E. coli(pCT66). To fulfil the requirements of a production system, a dual origin plasmid with controllable copy number was developed. Both this plasmid (pMG165) and a derivative which contained the prochymosin gene (pMG168) were stable when maintained at low copy number. When the copy number of plasmid pMG168 was increased by putting replication under the control of the lambda PR promoter and the cI857 temperature sensitive repressor, expression of prochymosin was achieved. This strategy enables large-scale production of prochymosin without the need for antibiotic selection or other methods of preventing plasmid loss.     

Expression of the human interferon alpha F gene in the obligate methylotroph Methylobacillus flagellatum KT and Pseudomonas putida

The expression of human leucocyte interferon alpha F gene in plasmid pLM-IFN alpha F-273 is controlled by a hybrid tac (trp-lac) promoter. A structural gene for interferon alpha F is a component of the hybrid operon lacZ'-IFN alpha F-TcR, that contains an E. coli trp-operon intercystronic region. Plasmid pLM IFN alpha F-273--directed interferon synthesis allows to obtain about 10(7) IU/l. This plasmid was cloned in broad-host-range vector plasmid pAYC31. The hybrid bi-repliconed plasmid containing interferon gene as well as its single-repliconed deletion derivatives obtained by the in vivo recombination, were introduced into obligate methylotroph Methylobacillus flagellatum KT and Pseudomonas putida PpG6. Methylotrophic strain and Pseudomonas were able to transcribe the interferon gene from E. coli tac promoter, the yield of interferon being 2-4-fold higher as compared with the one in the initial host.     

Influence of dilution rate and induction of cloned gene expression in continuous fermentations of recombinant yeast

The effects of growth rate on cloned gene product synthesis in recombinant Saccharomyces cerevisiae have been studied in continuous culture. The plasmid employed contains a yeast GAL10-CYC1 hybrid promoter directing expression of the E. coli lacZ gene. beta-Galactosidase production was therefore controlled by the yeast galactose regulatory circuit, and the induction process and its effects were studied at the various dilution rates. At all dilution rates plasmid stability decreased with induction of lacZ gene expression. In some instances, two induced "steady states" were observed, the first 10-15 residence times after induction and the second after 40-50 residence times. The second induced steady state was characterized by greater biomass concentration and lower beta-galactosidase specific activity relative to the first induced "steady-state." beta-Galactosidase specific activity and biomass concentration increased as dilution rate was reduced, and despite lower flow rate and plasmid stability, overall productivity (activity/L/hr) was substantially higher at low dilution rate. Important factors influencing all of the trends were the glucose and galactose (inducer) concentrations in the vessel and inducer metabolism.     

Control of acetate production rate in Escherichia coli by regulating expression of single-copy pta using lacI(Q) in multicopy plasmid

A tightly regulated gene expression system composed of a single-copy target gene under the control of a lac promoter derivative and lacI gene in a multicopy plasmid is proposed, and its ability to control the flux of a metabolic pathway is demonstrated. A model system to control the flux of acetyl-CoA to acetyl phosphate was constructed by integrating pta, a gene encoding phosphotransacetylase, under a tac promoter into the chromosome of E. coli with a pta-negative background and transforming a multicopy plasmid containing the lac iota(Q) gene into the strain. The production rate of acetate was shown to be tightly controlled when varying the concentration of the inducer (IPTG) in the model system.     

Effect of controlled expression of the hetR gene on heterocyst formation in the filamentous cyanobacterium Anabaena sp. PCC 7120

hetR is a central regulatory gene inducing and possibly maintaining irreversible heterocyst differentiation in filamentous cyanobacteria. A plasmid was constructed which enabled IPTG-mediated, controlled expression of hetR from a p _tac promoter in Anabaena . When introduced into a heterocyst-deficient hetR mutant, induction led to massive formation of heterocysts in a medium free of combined nitrogen. In nitrate-containing cultures, induction elicited formation of only a few heterocysts, but led to nitrogen chlorosis in vegetative cells as evidenced from degradation of phycobiliproteins. Removal of the inducer IPTG caused chlorosis and death of the organisms in nitrate-free medium, but no reversal of heterocyst formation. This indicates that constant synthesis of HetR is not the (sole) reason for irreversibility of heterocyst formation.     

重组有机磷水解酶MPH的发酵条件的优化研究

有机磷水解酶在去除有机磷农药残留中具有重要的应用前景。在Escherichia coli BL21(DE3)中实现了有机磷水解酶(MPH)的重组诱导表达之后,为了实现工业化生产MPH,考察了以乳糖为诱导剂,碳源、氮源、金属离子、培养温度、乳糖浓度及诱导时间等对产酶的影响,得到了优化的发酵条件,L9(34)正交实验进一步确定了最佳的碳源、氮源及乳糖浓度。在此基础上利用7L自控发酵罐进行了发酵过程研究,经12h培养,得到菌体12.65g(DCW)/L,MPH表达量为14.56%,酶活18.69I U/mL。     

Expression of a synthetic gene for human interleukin-4 in E. coli cells. Preparation of a biologically active protein]

Expression E. coli plasmid were constructed in which the human interleukin-4 (hIL4) synthetic gene is controlled by tac promoter. The expression level of the gene depends on the distance between RBS and the initial codon ATG, with the maximal production in case of the nine base pair distance. The recombinant protein, accumulated in the inclusion bodies, was solubilized, renaturated, and purified to homogeneous, biologically active preparation, the yield being 2 mg/g wet cells.     

Maximizing the expression of a recombinant gene in Escherichia coli by manipulation of induction time using lactose as inducer

Summary The use of isopropyl--d-thiogalactoside (IPTG) for induction of the lac-promoter in small-scale cultivations is well established. However, for large-scale microbiological processes the cost of this inducer is a severe limitation. Here is described a method by which lactose is used as inducer of the lac promoter with the same efficiency as that of IPTG. It was found that after growth on glucose the time of the addition of lactose is important for the quality of induction. the resulting yield of the recombinant protein increased when lactose was added to the culture if the glucose concentration was rather low. By careful monitoring of the glucose level in the fermentation, using a biosensor, it was possible to add the inducer when the carbon source was nearly depleted. Using Escherichia coli BL21 (pET3), in which was cloned the main antigen coat protein of the foot and mouth disease virus, induction of the gene led to expression of the target protein at a level exceeding 20% of the total cell protein.Offprint requests to: P. Neubauer     

Regulatable arabinose-inducible gene expression system with consistent control in all cells of a culture

The arabinose-inducible promoter P(BAD) is subject to all-or-none induction, in which intermediate concentrations of arabinose give rise to subpopulations of cells that are fully induced and uninduced. To construct a host-vector expression system with regulatable control in a homogeneous population of cells, the araE gene of Escherichia coli was cloned into an RSF1010-derived plasmid under control of the isopropyl-beta-D-thiogalactopyranoside-inducible P(tac) and P(taclac) promoters. This gene encodes the low-affinity, high-capacity arabinose transport protein and is controlled natively by an arabinose-inducible promoter. To detect the effect of arabinose-independent araE expression on population homogeneity and cell-specific expression, the gfpuv gene was placed under control of the arabinose-inducible araBAD promoter (P(BAD)) on the pMB1-derived plasmid pBAD24. The transporter and reporter plasmids were transformed into E. coli strains with native arabinose transport systems and strains deficient in one or both of the arabinose transport systems (araE and/or araFGH). The effects of the arabinose concentration and arabinose-independent transport control on population homogeneity were investigated in these strains using flow cytometry. The araE, and araE araFGH mutant strains harboring the transporter and reporter plasmids were uniformly induced across the population at all inducer concentrations, and the level of gene expression in individual cells varied with arabinose concentration. In contrast, the parent strain, which expressed the native araE and araFGH genes and harbored the transporter and reporter plasmids, exhibited all-or-none behavior. This work demonstrates the importance of including a transport gene that is controlled independently of the inducer to achieve regulatable and consistent induction in all cells of the culture.     

Purification of recombinant antigenic epitopes of the human 68-kDa (U1) ribonucleoprotein antigen using the expression system pH6EX3 followed by metal chelating affinity chromatography.

A novel plasmid expression vector (pH6EX3) that directs the synthesis of a fusion protein with a histidine hexapeptide at its N-terminus and a foreign protein at its C-terminus was constructed. The fusion gene is controlled by a strong tac promoter, leading to high-level expression of recombinant protein in several bacterial strains; the protein is deposited mainly as an insoluble mass in inclusion bodies. The fusion protein can be purified from the insoluble cell fraction by one-step affinity chromatography based on the selective interaction between the histidine hexapeptide and a metal chelating matrix charged with Ni2+ ions. The principle of this new system was tested by expressing and purifying antigenic epitopes of the human 68-kDa (U1) ribonucleoprotein autoantigen. With the use of column chromatography and pH gradient elution, about 25 micrograms recombinant protein/ml of bacterial culture was obtained.