Production of recombinant thermostable proteins expressed in Escherichia coli: completion of protein synthesis is the bottleneck

Heterologous expression and high yield purification of proteins are frequently required for structural and functional investigations. Purification of recombinant thermostable proteins is essentially trivial since unwanted mesophilic host protein can efficiently be removed by heat denaturation. However, heterologous expression in E. coli often results in truncated protein forms. In many cases, this is a consequence of abundant codons in heterologous genes, which are decoded by rare tRNAs in E. coli-a combination that can be responsible for translational stalling and termination during protein biosynthesis. Other complications may originate from potential initiation codons and ribosomal binding sites present inside the open reading frame of the target gene or from other less well defined phenomena such as mRNA instability. Separation of full-length protein from truncated forms is a serious chromatographic problem that can be solved in the expression step. We have investigated the heterologous expression and purification of two translation initiation factors from the hyperthermophilic sulphate-reducing archaeon, Archaeoglobus fulgidus. Expression in E. coli was optimised to avoid truncated forms completely by complementation with the plasmids pSJS1244, pRIG, pCODON+ and pLysSR.A.R.E harbouring and expressing genes encoding rare tRNAs corresponding to the codons AGA, AGG, AUA, CUA, GGA, AAG and CCC. Two expression strains, C41(DE3) and C43(DE3) were found highly advantageous when combined with rare tRNA encoding plasmids as compared to BL21(DE3). We have also investigated the effects of site directed mutagenesis on rare lysine encoding AAG doublets as well as two methionine residues preceded by potential ribosomal binding sites. The expression approach presented here has enabled us to purify gram quantities of full-length protein by one step of ion-exchange chromatography and is generally applicable to many other heterologously expressed thermostable proteins.     

Application of high-performance tangential flow filtration (HPTFF) to the purification of a human pharmaceutical antibody fragment expressed in Escherichia coli

High-performance tangential flow filtration (HPTFF) is shown to successfully enable concentration, purification and formulation in a single unit operation. This is illustrated with feedstreams comprising recombinant proteins expressed in Escherichia coli (E. coli). Using positively charged cellulosic membranes of 100 kDa molecular weight cut-off and operating under a selected range of buffer pH and ionic strength at a filtrate flux of 100 L m(-2) h(-1), a 10-fold removal of E. coli host cell proteins (HCP) was obtained with an overall process yield of 98%. The HPTFF performance was shown to be robust and reproducible. In addition, the novel charged membrane was regenerated and re-used seven times without loss of selectivity or throughput. When compared with a conventional purification scheme, the proposed process results in the elimination of one chromatographic step, a 12% yield improvement and a significant reduction in purification cost of goods.     

Adsorptive purification of pDNA on superporous rigid cross-linked cellulose matrix

Use of plasmid DNA (pDNA) in the emerging gene therapy requires pure DNA in large quantities requiring production of safe DNA on large scale. While a number of kit-based DNA purification techniques have become popular, large scale cost effective purification of DNA remains a technological challenge. Most traditional, as well as newly developed methods for DNA purification are expensive, tedious, use toxic reagents, and/or generally not amenable for scaled up production. Our attempts to develop a scalable adsorptive separation technology resulted in successful use of indigenously developed rigid cross-linked cellulose beads for single step purification of pDNA from alkaline cell lysates. This mode of purification employs a combination of intra-particle interactions that could give a product plasmid DNA free from chromosomal DNA, RNA and host proteins in a single scalable chromatographic step. The technology can be employed as a batch adsorption step on small scale, or on a large scale column chromatography. A high copy number 9.8 kb plasmid (from an Escherichia coli strain) was purified in yields of 77 and 52%, respectively in batch and column modes. The product obtained was homogeneous supercoiled plasmid with no RNA and protein contamination confirmed by quantitative analysis, agarose gel electrophoresis and SDS-PAGE.     

Purification of antibody and antibody-fragment from E. coli homogenate using 6,9-diamino-2-ethoxyacridine lactate as precipitation agent

To obtain a more efficient purification process for antibody fragments from an Escherichia coli homogenate, the precipitant, Ethodin (6,9-diamino-2-ethoxyacridine lactate) was introduced to the homogenate. By adding the precipitant a drastic reduction of host cell protein was obtained. The majority of the proteins were recovered in a precipitate with the cell debris, while the antibody or antibody-fragment was recovered in the clarified supernatant. In addition, DNA was also efficiently precipitated when using Ethodin as a precipitation agent. The improved purity of the clarified extract obtained by using the precipitant allows for the use of smaller chromatography columns and may reduce the number of chromatographic steps required in the recovery process. The effect of Ethodin concentration, pH, temperature, and conductivity were investigated. The investigation was performed on two different antibody-fragments, e.g., F(ab')(2) molecules and a full-length antibody produced in E. coli. The two F(ab')(2) proteins were F(ab')(2)A and F(ab')(2)B, which have a similar molecular mass (100 kDa) but different isoelectric points (pIs), i.e., 8.9 and 7.5, respectively. The full-length antibody, Ab (the full IgG form of F(ab')(2)B) has a pI of 7.8 and molecular mass of 150 kDa. The investigation showed that the highest purification factors were obtained at neutral pH, low conductivity, and Ethodin concentrations of 0.6%.     

Growth and productivity impacts of periplasmic nuclease expression in an Escherichia coli Fab' fragment production strain

Host cell engineering is becoming a realistic option in whole bioprocess strategies to maximize product manufacturability. High molecular weight (MW) genomic DNA currently hinders bioprocessing of Escherichia coli by causing viscosity in homogenate feedstocks. We previously showed that co-expressing Staphylococcal nuclease and human Fab' fragment in the periplasm of E. coli enables auto-hydrolysis of genomic DNA upon cell disruption, with a consequent reduction in feedstock viscosity and improvement in clarification performance. Here we report the impact of periplasmic nuclease expression on stability of DNA and Fab' fragment in homogenates, host-strain growth kinetics, cell integrity at harvest and Fab' fragment productivity. Nuclease and Fab' plasmids were shown to exert comparable levels of growth burden on the host W3110 E. coli strain. Nuclease co-expression did not compromise either the growth performance or volumetric yield of the production strain. 0.5 g/L Fab' fragment (75 L scale) and 0.7 g/L (20 L scale) was achieved for both unmodified and cell-engineered production strains. Unexpectedly, nuclease-modified cells achieved maximum Fab' levels 8-10 h earlier than the original, unmodified production strain. Scale-down studies of homogenates showed that nuclease-mediated hydrolysis of high MW DNA progressed to completion within minutes of homogenization, even when homogenates were chilled on ice, with no loss of Fab' product and no need for additional co-factors or buffering.     

Design, production, and characterization of an engineered biotin ligase (BirA) and its application for affinity purification of staphylokinase produced from Bacillus subtilis via secretion

A major attraction in using Bacillus subtilis as an expression host for heterologous protein production is its ability to secrete extracellular proteins into the culture medium. To take full advantage of this system, an efficient method for recovering the target protein is crucial. For secretory proteins which cannot be purified by a simple scheme, in vitro biotinylation using biotin ligase (BirA) offers an effective alternative for their purification. The availability of large amounts of quality BirA can be critical for in vitro biotinylation. We report here the engineering and production of an Escherichia coli BirA and its application in the purification of staphylokinase, a fibrin-specific plasminogen activator, from the culture supernatant of Bacillus subtilis via in vitro biotinylation. BirA was tagged with both a chitin-binding domain and a hexahistidine tail to facilitate both its purification and its removal from the biotinylated sample. We show in this paper how, in a unique way, we solved the problem of protein aggregation in the E. coli BirA production system to achieve a yield of soluble functional BirA hitherto unreported in the literature. Application of this novel BirA to protein purification via in vitro biotinylation in general will also be discussed. Biotinylated staphylokinase produced in the study not only can act as an intermediate for easy purification, it can also serve as an important element in the creation of a blood clot targeting and dissolving agent.     

Single step purification of plasmid DNA using peptide ligand affinity chromatography

Single step affinity chromatography was employed for the purification of plasmid DNA (pDNA), thus eliminating several steps compared with current commercial purification methods for pDNA. Significant reduction in pDNA production time and cost was obtained. This chromatographic operation employed a peptide-monolith construct to isolate pDNA from Escherichia coli (E. coli) impurities present in a clarified lysate feedstock. Mild conditions were applied to avoid any degradation of pDNA. The effect of some important parameters on pDNA yield was also evaluated with the aim of optimising the affinity purification of pDNA. The results demonstrate that 81% of pDNA was recovered and contaminating gDNA, RNA and protein were removed below detectable levels.     

Expression and purification of His-tagged HPV16 E7 protein active in pRb binding

Human papillomavirus type 16 (HPV16) protein E7 is the major oncogenic factor associated with the development of human cervical cancer. The transforming activity of the E7 protein is linked to its interaction with host regulatory proteins such as the retinoblastoma tumor suppressor protein. The recombinant production of E7 protein is a prerequisite for its structural and functional characterization as well as for the development of various preventive and therapeutic strategies. We present an approach to enhance the soluble expression of His-tagged E7 protein by optimization of the E7 gene and the expression conditions in the host Escherichia coli. We also report a detailed protocol for the purification of E7 protein by standard chromatographic methods. The binding of E7 protein to the recombinant non-phosphorylated form of retinoblastoma protein was examined by ELISA and surface plasmon resonance analysis. These studies confirm that the recombinant His-tagged E7 protein retains its conformational properties and biological activity.     

Optimization of the production and purification processes of carnobacteriocins Cbn BM1 and Cbn B2 from Carnobacterium maltaromaticum CP5 by heterologous expression in Escherichia coli

An optimization of the production and purification processes of carnobacteriocins Cbn BM1 and Cbn B2 from Carnobacterium maltaromaticum CP5, by heterologous expression in Escherichia coli is described. The genes encoding mature bacteriocin were cloned into an E. coli expression system and expressed as a fusion protein with a thermostable thioredoxin. Recombinant E. coli were cultivated following a fed-batch fermentation process with pH, temperature and oxygenation regulation. The overexpression of the fusion proteins was improved by replacing IPTG by lactose. The fusion proteins were purified by thermal coagulation followed by affinity chromatography. The thioredoxin fusion protein was removed by using CNBr instead of enterokinase and the carnobacteriocins were recovered by reverse-phase chromatography. These optimizations led us to produce up to 320 mg of pure protein per liter of culture, which is four to ten fold higher than what is described for other heterologous expression systems.     

Purification of recombinant brain derived neurotrophic factor using reversed phase displacement chromatography

This work investigates the utility of RPLC displacement chromatography for the purification of recombinant brain derived neurotrophic factor (rHu-BDNF) from its variants and E. coli. protein (ECP) impurities. The closely associated variants (six in total) differ by one amino acid from the native BDNF and thus pose a challenging separation problem. Several operational parameters were investigated to study their effects on the yield of the displacement process. The results indicated that the concentration of trifluoroacetic acid (TFA) in the buffer was a key factor in achieving the desired purification. Displacement chromatography on an analytical scale column resulted in extremely high purity and yield in a single chromatographic step. The process was successfully scaled-up with respect to particle and column diameter. The production rate of a pilot scale RPLC displacement process was shown to be 23 times higher than the combined production rates of the current preparative ion exchange and hydrophobic interaction gradient elution steps that are used to remove variant and ECP impurities, respectively.     

Use of ZetaPrep cartridge for the purification of human recombinant interleukin 1 beta

Zetaprep mass ion-exchange media represent a rapid and efficient chromatographic tool in the separation of proteins, in place of the conventional agarose or cellulose-based gels. We adopted this method, combined with classical steps, to purify to homogeneity human recombinant interleukin 1 beta (IL-1 beta) produced from E. coli and from S. cerevisiae. An anion exchanger QAE-ZetaPrep was used to achieve a rapid partial purification of both proteins. The IL-1 beta purification was completed by gel permeation chromatography on Sephadex G-50. When the protein was produced from yeast, an intermediate chromatographic step on a hydroxylapatite column was also necessary. The isolated proteins proved to be homogeneous by electrophoresis and amino acid analysis. The biological activity of IL-1 beta produced by E. coli is comparable to that of the natural protein, while the protein produced by yeast showed very low specific activity.     

High-level overproduction of <Emphasis Type="Italic">Thermus</Emphasis> enzymes in <Emphasis Type="Italic">Streptomyces lividans</Emphasis>

Biotechnology needs to explore the capacity of different organisms to overproduce proteins of interest at low cost. In this paper, we show that Streptomyces lividans is a suitable host for the expression of Thermus thermophilus genes and report the overproduction of the corresponding proteins. This capacity was corroborated after cloning the genes corresponding to an alkaline phosphatase (a periplasmic enzyme in T. thermophilus) and that corresponding to a beta-glycosidase (an intracellular enzyme) in Escherichia coli and in S. lividans. Comparison of the production in both hosts revealed that the expression of active protein achieved in S. lividans was much higher than in E. coli, especially in the case of the periplasmic enzyme. In fact, the native signal peptide of the T. thermophilus phosphatase was functional in S. lividans, being processed at the same peptide bond in both organisms, allowing the overproduction and secretion of this protein to the S. lividans culture supernatant. As in E. coli, the thermostability of the expressed proteins allowed a huge purification factor upon thermal denaturation and precipitation of the host proteins. We conclude that S. lividans is a very efficient and industry-friendly host for the expression of thermophilic proteins from Thermus spp.     

Extracellular production of recombinant proteins using bacterial autotransporters

Escherichia coli is still a very popular host for the production of recombinant proteins at an analytical or industrial scale. Secretion of the proteins into the culture medium or display at the cell surface would be preferred in many applications but is hampered by the complex two-layered cell envelope. The autotransporter pathway is used by E. coli to secrete virulence factors via a relatively simple but efficient and specific mechanism. Here we discuss recent progress in the structural and mechanistic analysis of this pathway and the implications for future development of a versatile platform for secretion and display of heterologous proteins.     

Improving the production of E. coli beta-lactamase in Bacillus subtilis: the effect of glucose, pH and temperature on the production level.

Bacillus subtilis has been considered a promising host for the production of foreign proteins. However, proteases released by the host organism can often cause rapid breakdown of secreted heterologous proteins. Here we report that the addition of 6% glucose and 100 mM potassium phosphate to the growth medium significantly reduces the degradation of E. coli TEM beta-lactamase secreted from B. subtilis, when applying an expression system based on B. amyloliquefaciens alpha-amylase. The yield of beta-lactamase was increased 10-20-fold when compared to the yield in Luria medium. The promoter of B. amyloliquefaciens alpha-amylase gene is repressed by glucose. However, here we show that the repression does not take place in a multicopy plasmid, thus enabling our approach to efficiently reduce the protease action by catabolite repression. We have also studied the role of pH and temperature on the beta-lactamase production in laboratory scale bioreactors. Low temperature and low pH are both favorable for a high level beta-lactamase production by the high copy plasmid construction.     

Cloning, expression, and characterization of the Anabaena thioredoxin gene in Escherichia coli.

The gene encoding thioredoxin in Anabaena sp. strain PCC 7119 was cloned in Escherichia coli based on the strategy that similarity between the two thioredoxins would be reflected both in the gene sequence and in functional cross-reactivity. DNA restriction fragments containing the Anabaena thioredoxin gene were identified by heterologous hybridization to the E. coli thioredoxin gene following Southern transfer, ligated with pUC13, and used to transform an E. coli strain lacking functional thioredoxin. Transformants that complemented the trxA mutation in E. coli were identified by increased colony size and confirmed by enzyme assay. Expression of the cloned Anabaena thioredoxin gene in E. coli was substantiated by subsequent purification and characterization of the algal protein from E. coli. The amino acid sequence derived from the DNA sequence of the Anabaena gene was identical to the known amino acid sequence of Anabaena thioredoxin. The E. coli strains which expressed Anabaena thioredoxin complemented the TrxA- phenotype in every respect except that they did not support bacteriophage T7 growth and had somewhat decreased ability to support bacteriophages M13 and f1.     

Heterologous protein expression is enhanced by harmonizing the codon usage frequencies of the target gene with those of the expression host

Synonymous codon replacement can change protein structure and function, indicating that protein structure depends on DNA sequence. During heterologous protein expression, low expression or formation of insoluble aggregates may be attributable to differences in synonymous codon usage between expression and natural hosts. This discordance may be particularly important during translation of the domain boundaries (link/end segments) that separate elements of higher ordered structure. Within such regions, ribosomal progression slows as the ribosome encounters clusters of infrequently used codons that preferentially encode a subset of amino acids. To replicate the modulation of such localized translation rates during heterologous expression, we used known relationships between codon usage frequencies and secondary protein structure to develop an algorithm ("codon harmonization") for identifying regions of slowly translated mRNA that are putatively associated with link/end segments. It then recommends synonymous replacement codons having usage frequencies in the heterologous expression host that are less than or equal to the usage frequencies of native codons in the native expression host. For protein regions other than these putative link/end segments, it recommends synonymous substitutions with codons having usage frequencies matched as nearly as possible to the native expression system. Previous application of this algorithm facilitated E. coli expression, manufacture and testing of two Plasmodium falciparum vaccine candidates. Here we describe the algorithm in detail and apply it to E. coli expression of three additional P. falciparum proteins. Expression of the "recoded" genes exceeded that of the native genes by 4- to 1,000-fold, representing levels suitable for vaccine manufacture. The proteins were soluble and reacted with a variety of functional conformation-specific mAbs suggesting that they were folded properly and had assumed native conformation. Codon harmonization may further provide a general strategy for improving the expression of soluble functional proteins during heterologous expression in hosts other than E. coli.     

Functional expression in Escherichia coli of proteins B and C from soluble methane monooxygenase of Methylococcus capsulatus (Bath).

Methylococcus capsulatus (Bath) uses a soluble methane monooxygenase (sMMO) to catalyse the oxidation of methane to methanol. sMMO is comprised of three components; A, B and C. Protein C (the reductase) transfers electrons from NADH to protein A (the hydroxylase) which contains the active site, and protein B regulates this electron flow. The five genes encoding the sMMO proteins and their subunits are clustered and have been cloned in Escherichia coli. A DNA fragment containing mmoB, the gene encoding protein B, was subcloned into pT7-5, a plasmid of the T7 RNA polymerase promoter expression system. Upon induction, E. coli expressed protein B which was fully functional after purification. The gene encoding protein C, mmoC, was amplified with unique restriction sites at each end using the polymerase chain reaction and then subcloned into pT7-7 (a plasmid similar to pT7-5 but containing its own ribosome-binding site and ATG start codon). Protein C expressed in E. coli was also found to be functional. This is the first report of the functional expression of methanotroph methane monooxygenase genes in a heterologous host and represents a significant step forward in our analysis of the assembly and catalysis of sMMO.     

pCold-GST vector: a novel cold-shock vector containing GST tag for soluble protein production

The production of recombinant protein in Escherichia coli is often hampered by low expression levels and low solubility. A variety of methodologies have been developed including protein production at low temperature, and fusion protein expression using soluble protein tags. Here, we present the novel cold-shock vector pCold-GST for high-level expression of soluble proteins in E. coli. This vector is a modified pCold I cold-shock vector that includes the glutathione S-transferase (GST) tag. The pCold-GST expression system developed was applied to 10 proteins that could not be expressed using conventional E. coli expression methodologies, and nine of these proteins were successfully obtained in the soluble fraction. The expression and purification of two unstable protein fragments were also demonstrated by employing a C-terminal hexa-histidine tag for purification purposes. The purified proteins were amenable to NMR analyses. These data suggest that the pCold-GST expression system can be utilized to improve the expression and purification of various proteins.