Elevated Fis expression enhances recombinant protein production in Escherichia coli

A genetic strategy to enhance recombinant protein production is discussed. A small DNA bending protein, Fis, which has been shown to activate rRNA synthesis upon a nutrient upshift, was overexpressed in E. coli strain W3110 carrying vector pUCR1. Overexpression of Fis during exponential growth was shown to activate rrn promoters to different extents. A 5-fold improvement in chloramphenicol acetyltransferase (CAT) production in cultures with elevated Fis level was observed in shake-flask cultivations. A similar improvement in the culture performance was also observed during fed-batch fermentation; the specific CAT activity increased by more than 50% during the fed-batch phase for cultures with elevated Fis expression. In contrast, no increase in specific CAT activity was detected for cultures carrying pUCR2, expressing a frame-shift Fis mutant. Expression of Fis from a complementary vector, pKFIS, restored CAT production from W3110:pUCR2 to approximately the same level as cultures carrying pUCR1, indicating that the enhancement in CAT production was indeed Fis-dependent. The framework presented here suggests that differential activation in recombinant protein production may be achieved with differential Fis overexpression. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 56: 138-144, 1997.     

Polyhydroxyalkanoate production in recombinant Escherichia coli

Abstract The bacterial species Escherichia coli has proven to be a powerful tool in the molecular analysis of polyhydroxyalkanoate (PHA) biosynthesis. In addition, E. coli holds promise as a source for economical PHA production. Using this microorganism, clones have been developed in our laboratory which direct the synthesis of poly-β-hydroxybutyrate (PHB) to levels as high as 95% of the cell dry weight. These clones have been further enhanced by the addition of a genetically mediated lysis system that allows the PHB granules to be released gently and efficiently. This paper describes these developments, as well as the use of an E. coli strain to produce the copolymer poly-(3-hydroxybutyrate- co -3-hydroxyvalerate (PHB- co -3-).     

Quantification of metabolic limitations during recombinant protein production in Escherichia coli

Escherichia coli is one of the major microorganisms for recombinant protein production because it has been best characterized in terms of molecular genetics and physiology, and because of the availability of various expression vectors and strains. The synthesis of proteins is one of the most energy consuming processes in the cell, with the result that cellular energy supply may become critical. Indeed, the so called metabolic burden of recombinant protein synthesis was reported to cause alterations in the operation of the host's central carbon metabolism.To quantify these alterations in E. coli metabolism in dependence of the rate of recombinant protein production, ¹³C-tracer-based metabolic flux analysis in differently induced cultures was used. To avoid dilution of the ¹³C-tracer signal by the culture history, the recombinant protein produced was used as a flux probe, i.e., as a read out of intracellular flux distributions. In detail, an increase in the generation rate rising from 36 mmol_ATP g_CDW⁻¹ h⁻¹ for the reference strain to 45 mmol_ATP g_CDW⁻¹ h⁻¹ for the highest yielding strain was observed during batch cultivation. Notably, the flux through the TCA cycle was rather constant at 2.5 ± 0.1 mmol g_CDW⁻¹ h⁻¹, hence was independent of the induced strength for gene expression. E. coli compensated for the additional energy demand of recombinant protein synthesis by reducing the biomass formation to almost 60%, resulting in excess NADPH. Speculative, this excess NADPH was converted to NADH via the soluble transhydrogenase and subsequently used for ATP generation in the electron transport chain. In this study, the metabolic burden was quantified by the biomass yield on ATP, which constantly decreased from 11.7 g_CDW mmol_ATP⁻¹ for the reference strain to 4.9 g_CDW mmol_ATP⁻¹ for the highest yielding strain. The insights into the operation of the metabolism of E. coli during recombinant protein production might guide the optimization of microbial hosts and fermentation conditions.     

High-level recombinant protein production by overexpression of Mlc in Escherichia coli

Escherichia coli excretes acetate during aerobic growth on LB broth containing glucose and growth ceases before depletion of glucose because of the low pH caused by the accumulation of acetate. It has been known that the acetate accumulation is reduced even when E. coli is grown in the presence of high concentration of glucose if Mlc is overexpressed. The intracellular concentration of Mlc is very low in E. coli because of autoregulation and a low efficiency of mlc translation. We constructed various mutants that can express higher levels of Mlc using site-directed mutagenesis and one of the Mlc-overproducing mutant showed reduced glucose consumption rate and low production of acetate. The mutant showed higher foreign gene expression level than that of its parental strain in the presence of glucose. These results suggest that the Mlc overproducing E. coli strain having an improved ability of glucose utilization can be a better host for high-level production of useful recombinant proteins.     

Enhancement of recombinant protein production in Escherichia coli by coproduction of aspartase

As commonly recognized, the excretion of acetate by the aerobic growth of Escherichia coli on glucose is a manifestation of imbalanced flux between glycolysis and the tricarboxylic acid (TCA) cycle. Accordingly, this may restrict the production of recombinant proteins in E. coli, due to the limited amounts of precursor metabolites produced in TCA cycle. To approach this issue, an extra supply of intermediate metabolites in TCA cycle was made by conversion of aspartate to fumarate, a reaction mediated by the activity of L-aspartate ammonia-lyase (aspartase). As a result, in the glucose minimal medium containing aspartate, the production of two recombinant proteins, beta-galactosidase and green fluorescent protein, in the aspartase-producing strain was substantially increased by 5-fold in association with 30-40% more biomass production. This preliminary study illustrates the great promise of this approach used to enhance the production of these two recombinant proteins.     

Polyhydroxyalkanoate production in recombinant Escherichia coli.

The bacterial species Escherichia coli has proven to be a powerful tool in the molecular analysis of polyhydroxyalkanoate (PHA) biosynthesis. In addition, E. coli holds promise as a source for economical PHA production. Using this microorganism, clones have been developed in our laboratory which direct the synthesis of poly-beta-hydroxybutyrate (PHB) to levels as high as 95% of the cell dry weight. These clones have been further enhanced by the addition of a genetically mediated lysis system that allows the PHB granules to be released gently and efficiently. This paper describes these developments, as well as the use of an E. coli strain to produce the copolymer poly-(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHB-co-3HV).     

A synthetic biology approach to self-regulatory recombinant protein production in Escherichia coli

Background

Recombinant protein production is a process of great industrial interest, with products that range from pharmaceuticals to biofuels. Since high level production of recombinant protein imposes significant stress in the host organism, several methods have been developed over the years to optimize protein production. So far, these trial-and-error techniques have proved laborious and sensitive to process parameters, while there has been no attempt to address the problem by applying Synthetic Biology principles and methods, such as integration of standardized parts in novel synthetic circuits.

Results

We present a novel self-regulatory protein production system that couples the control of recombinant protein production with a stress-induced, negative feedback mechanism. The synthetic circuit allows the down-regulation of recombinant protein expression through a stress-induced promoter. We used E. coli as the host organism, since it is widely used in recombinant processes. Our results show that the introduction of the self-regulatory circuit increases the soluble/insoluble ratio of recombinant protein at the expense of total protein yield. To further elucidate the dynamics of the system, we developed a computational model that is in agreement with the observed experimental data, and provides insight on the interplay between protein solubility and yield.

Conclusion

Our work introduces the idea of a self-regulatory circuit for recombinant protein products, and paves the way for processes with reduced external control or monitoring needs. It demonstrates that the library of standard biological parts serves as a valuable resource for initial synthetic blocks that needs to be further refined to be successfully applied in practical problems of biotechnological significance. Finally, the development of a predictive model in conjunction with experimental validation facilitates a better understanding of the underlying dynamics and can be used as a guide to experimental design.     

Extracellular recombinant protein production from an Escherichia coli lpp deletion mutant

E. coli is one of the most commonly used host strains for recombinant protein production. However, recombinant proteins are usually found intracellularly, in either cytoplasm or periplasmic space. Inadequate secretion to the extracellular environment is one of its limitations. This study addresses the outer membrane barrier for the translocation of recombinant protein directed to the periplasmic space. Specifically, using recombinant maltose binding protein (MalE), xylanase, and cellulase as model proteins, we investigated whether the lpp deletion could render the outer membrane permeable enough to allow extracellular protein production. In each case, significantly higher excretion of recombinant protein was observed with the lpp deletion mutant. Up to 90% of the recombinant xylanase activity and 70% of recombinant cellulase activity were found in the culture medium with the deletion mutant, whereas only 40-50% of the xylanase and cellulase activities were extracellular for the control strain. Despite the weakened outer membrane in the mutant strain, cell lysis did not occur, and increased excretion of periplasmic protein was not due to cell lysis. The lpp deletion is a simple method to generate an E. coli strain to effect significant extracellular protein production. The phenotype of extracellular protein production without cell lysis is useful in many biotechnological applications, such as bioremediation and plant biomass conversion.     

The production of polyhydroxyalkanoates in recombinant Escherichia coli

Polyhydroxyalkanoates, the natural polyester that many microorganisms accumulate to store carbon and reducing equivalents, have been considered as a future alternative of traditional plastic due to their special properties. In Escherichia coli, a previous non-polyhydroxyalkanoates producer, pathway engineering has been developed as a very powerful approach to set up microbial production process through the introduction of direct genetic changes by recombinant DNA technology. Various metabolic pathways leading to the polyhydroxyalkanoates accumulation with desirable properties at low-cost and high-productivity have been developed. At the same time, high density fermentation technology of E. coli provides an efficient polyhydroxyalkanoates production strategy. This review focused on metabolic engineering, fermentation and downstream process aiming to polyhydroxyalkanoates production in E. coli.     

Effects of glycine supplement on protein production and release in recombinant Escherichia coli

Summary The effect of glycine supplement to growth media on protein expression and release in a recombinant strain RR1 of E. coli was investigated. Addition of glycine to the growth media in moderate amount (up to 1%) was observed to enhance significantly the release of periplasmic proteins from the cell to the broth. The extracellular activities of the model enzymes -amylase and -lactamase were increased by a factor of 16.3 and 3.8 respectively in the presence of glycine. These activities corresponded to about 50% of the total production for each protein. Furthermore, with glycine supplement the total enzyme activity of both -amylase, -lactamase as well as -galactosidase were increased by a factor of about 2.5. Cell growth characteristics and low extracellular activity of the cytoplasmic protein -galactosidase are indicative that glycine does not cause significant cell-lysis for a concentration below 0.7%.     

Combinatorial expression vector engineering for tuning of recombinant protein production in Escherichia coli

The complex and integrated nature of both genetic and protein level factors influencing recombinant protein production in Escherichia coli makes it difficult to predict the optimal expression strategy for a given protein. Here, two combinatorial library strategies were evaluated for their capability of tuning recombinant protein production in the cytoplasm of E. coli. Large expression vector libraries were constructed through either conservative (ExLib1) or free (ExLib2) randomization of a seven-amino-acid window strategically located between a degenerated start codon and a sequence encoding a fluorescently tagged target protein. Flow cytometric sorting and analyses of libraries, subpopulations or individual clones were followed by SDS-PAGE, western blotting, mass spectrometry and DNA sequencing analyses. For ExLib1, intracellular accumulation of soluble protein was shown to be affected by codon specific effects at some positions of the common N-terminal extension. Interestingly, for ExLib2 where the same sequence window was randomized via seven consecutive NN(G/T) tri-nucleotide repeats, high product levels (up to 24-fold higher than a reference clone) were associated with a preferential appearance of novel SD-like sequences. Possible mechanisms behind the observed effects are discussed.     

Reduction of acetate accumulation in Escherichia coli cultures for increased recombinant protein production

The culture of Escherichia coli for the commercial production of recombinant proteins has increased significantly in recent years. The production of acetate as a byproduct retards cell growth, inhibits protein formation, and diverts carbon from biomass to protein product. Our approach to reducing acetate accumulation was to disable the phosphoenolpyruvate:sugar phosphotransferase system (PEP-PTS) by deleting the ptsHI operon in the wild-type E. coli strain GJT001. The mutation caused a severe reduction in growth rate and glucose uptake rate in glucose-supplemented M9 minimal medium, which confirmed the mutation, and eliminated acetate accumulation. The mutant strain (TC110) apparently metabolized glucose by a non-PTS mechanism that we are currently investigating, followed by phosphorylation by glucokinase. In complex medium such as 2xLB broth with 2% glucose, TC110 was able to grow quickly and still retained the phenotype of significantly reduced acetate accumulation (9.1+/-6.6 vs. 90.4+/-1.6mM in GJT001, P<0.05). The reduced acetate accumulation resulted in a significant improvement in final OD (23.5+/-0.7 in TC110 vs. 8.0+/-0.1 in GJT001, P<0.05). We tested the strains for the production of model recombinant proteins such as green fluorescent protein (GFP) and beta-galactosidase. TC110 had a 385-fold improvement in final volumetric productivity of GFP over GJT001 in shake flasks with 2xLB broth with 2% glucose. The distribution of GFP fluorescence in the cell population, as determined by flow cytometry, was much broader in GJT001 (coefficient of variation=466+/-35%) than in TC110 (coefficient of variation=55+/-1%). In corn steep liquor medium with 2% glucose, we observed a 28.5-fold improvement in final volumetric production of GFP in TC110 over GJT001. TC110 had a 7.5-fold improvement in final volumetric productivity of beta-galactosidase over GJT001 in 2xLB broth with 2% glucose medium. When tested in a batch bioreactor cultures with 2xLB broth with 2% glucose medium, the volumetric production of GFP by TC110 was 25-fold higher than that of GJT001. In summary, the ptsHI mutant of GJT001 resulted in reduced acetate accumulation, which led to significant improvements in recombinant protein production in batch bioreactors.     

Genetic manipulation of stationary-phase genes to enhance recombinant protein production in Escherichia coli

Genetic manipulation of the host strain, by which cell physiology could be modulated, was exploited to enhance recombinant protein production in Escherichia coli. The effects of an inactivated stationary-phase gene (rmf or katF) on recombinant protein production in strains with two different expression systems (the pH-inducible and the lac promoters) were investigated. An improvement of recombinant protein production in the katF mutant at low growth rates was observed for both expression systems. A fourfold and a 30% increase in the volumetric recombinant protein activity were observed for the pH-inducible and the lac promoter system, respectively. The effect of the rmf mutation, on the other hand, depends on the expression system. A twofold increase in the volumetric recombinant protein activity was found for the pH-inducible promoter system, but there was no improvement for the lac promoter system. Improvement in culture performance for slow-growing cultures may have an impact on the design strategy of the host/vector system used in fed-batch cultures, where the specific growth rate is usually slow. The information may also be useful for developing optimal host/vector gene expression systems for recombinant protein production. (c) 1996 John Wiley & Sons, Inc.     

Scale-up of recombinant Opc protein production in Escherichia coli for a meningococcal vaccine

Opc is an outer membrane protein from Neisseria meningitidis present in meningococcal vaccine preparations. The opc gene, codifying for this protein, was cloned in to Escherichia coli and the Opc protein was expressed under the control of a tryptophan promoter. The recombinant strain was grown in batch cultures. Opc was expressed as inclusion bodies at about 32% of the total cellular protein. We examined the scale-up culture conditions for the production of the recombinant Opc. The scale-up process was performed from 1.5 l to 50 l culture, using first, the constant power per unit of volume (P/V) as main scaling criteria, and then the oxygen mass transfer coefficient (K(L)a) scaling criteria to adjust the optimal aeration conditions. A final productivity of 52 mgl(-1)h(-1) was obtained at the 50l culture scale compared with the 49 mgl(-1)h(-1) productivity at 1.5l laboratory scale.     

Recombinant protein production in Escherichia coli

Growing needs for efficient recombinant production pose new challenges; starting from cell growth optimization under overexpression conditions, improving vectors, gene and protein sequence to suit them to protein biosynthesis machinery of the host, through extending the knowledge of protein folding, fusion protein construction, and coexpression systems, to improvements in protein purification and renaturation technologies. Hitherto Escherichia coli is the most defined and the cheapest protein biosynthesis system. With its wealth of available mutants tested is the best suited to economically test new gene constructs and to scale up the recombinant protein production.     

Optimum melanin production using recombinant Escherichia coli

AIMS: A parametric study was conducted to define optimum conditions to achieve high yields in the conversion of tyrosine to eumelanin (EuMel) using recombinant Escherichia coli. METHODS AND RESULTS: Escherichia coli W3110 (pTrcMutmelA) expressing the tyrosinase coding gene from Rhizobium etli and glucose-mineral media were used to transform tyrosine into EuMel. Batch aerobic fermentor cultures were performed to study the effect of temperature, pH and inducer concentration (isopropyl-D-thio-galactopyranoside) on melanin production. Under optimum conditions, 0.1 mmol l(-1) of isopropyl-D-thio-galactopyranoside, temperature of 30 degrees C, and changing pH from 7.0 to 7.5 during the production phase, a 100% conversion of tyrosine into EuMel is obtained. Furthermore, tyrosine feeding allowed us to obtain the highest level (6 g l(-1)) of EuMel produced by recombinant E. coli reported until now. CONCLUSIONS: The most important factors affecting melanin formation and hence influencing the rate and efficiency in the conversion of tyrosine into EuMel in this system, are the temperature and pH. SIGNIFICANCE AND IMPACT OF THE STUDY: Maximum theoretical yield was obtained using a simple culture process and mineral media to convert tyrosine (a medium value compound) into melanin, a high value compound. The process reported here avoids the use of purified tyrosinase, expensive chemical methods or the cumbersome extraction of this polymer from animal or plant tissues.