High-level transient expression of recombinant protein in lettuce

Transient expression following agroinfiltration of plant tissue was investigated as a system for producing recombinant protein. As a model system, Agrobacterium tumefaciens containing the beta-glucuronidase (GUS) gene was vacuum infiltrated into lettuce leaf disks. Infiltration with a suspension of 10(9) colony forming units/mL followed by incubation for 72 h at 22 degrees C in continuous darkness produced a maximum of 0.16% GUS protein based on dry tissue or 1.1% GUS protein based on total soluble protein. This compares favorably to expression levels for commercially manufactured GUS protein from transgenic corn seeds. A. tumefaciens culture medium pH between 5.6 and 7.0 and surfactant concentrations < or = 100 ppm in the vacuum infiltration did not affect GUS expression, while infiltration with an A. tumefaciens density of 10(7) and 10(8) colony forming units/mL, incubation at 29 degrees C, and a surfactant concentration of 1,000 ppm significantly reduced expression. Incubation in continuous light caused lettuce to produce GUS protein more rapidly, but final levels did not exceed the GUS production in leaves incubated in continuous darkness after 72 h at 22 degrees C. The kinetics of GUS expression during incubation in continuous light and dark were represented well using a logistic model, with rate constants of 0.30 and 0.29/h, respectively. To semi-quantitatively measure the GUS expression in large numbers of leaf disks, a photometric enhancement of the standard histochemical staining method was developed. A linear relationship with an R2 value of 0.90 was determined between log10 (% leaf darkness) versus log10 (GUS activity). Although variability in expression level was observed, agroinfiltration appears to be a promising technology that could potentially be scaled up to produce high-value recombinant proteins in planta.     

High-level expression of recombinant human FK-binding protein from a fusion precursor

The human peptidyl-prolyl isomerase FK-binding protein (FKBP) was cloned as a fusion partner with CMP-KDO synthetase (CKS), and the resultant construct was characterized as an improved high-expression source for FKBP. The CKS-FKBP fusion was expressed as a soluble protein at levels approaching 1 gm/L inEscherichia coli fermentations. The fusion protein was purified to near homogeneity by a one-step ammonium sulfate fractionation of whole cell lysate. After selective cleavage, the fusion precursor produced yields approaching 300 mg of purified FKBP per liter of harvested culture, a 30 to 60-fold increase over that observed for a nonfusion construct. Selective cleavage of the fusion partners was accomplished using either hydroxylamine or specific, limited proteolysis. Once separated from the CKS fusion partner, the FKBP was isolated in a single step by either reversed-phase HPLC or chromatography on Q-Sepharose. For comparison of physical and chemical properties, a nonfusion construct of recombinant human FKBP was expressed inE. coli and isolated. The purified FKBPs exhibited expected SDS-PAGE molecular weights and N-terminal sequences. The proteins had similar proton NMR spectra and binding to [³H]FK-506. The fusion construct, CKS-FKBP, was also found to bind [³H]FK-506. These data indicate that FKBP fused to the C-terminus of CKS folds independently of the fusion partner and suggests the fused FKBP adopts a conformation resembling that of the native protein.     

Tuning recombinant protein expression to match secretion capacity

Background

The secretion of recombinant disulfide-bond containing proteins into the periplasm of Gram-negative bacterial hosts, such as E. coli, has many advantages that can facilitate product isolation, quality and activity. However, the secretion machinery of E. coli has a limited capacity and can become overloaded, leading to cytoplasmic retention of product; which can negatively impact cell viability and biomass accumulation. Fine control over recombinant gene expression offers the potential to avoid this overload by matching expression levels to the host secretion capacity.

Results

Here we report the application of the RiboTite gene expression control system to achieve this by finely controlling cellular expression levels. The level of control afforded by this system allows cell viability to be maintained, permitting production of high-quality, active product with enhanced volumetric titres.

Conclusions

The methods and systems reported expand the tools available for the production of disulfide-bond containing proteins, including antibody fragments, in bacterial hosts.

     

High-level expression and secretion of recombinant mouse endostatin by Escherichia coli

The expression of murine endostatin was achieved by placing its gene downstream of an alkaline phosphatase gene (phoA) promoter. To ensure proper folding and secretion of the recombinant protein, the mouse endostatin was fused with alkaline phosphatase signal peptide. SDS/polyacrylamide gel electrophoresis analysis of the culture medium of recombinant Escherichia coli cells revealed that endostatin was efficiently secreted. The signal peptide was efficiently cleaved during secretion as demonstrated by N-terminal amino acid sequencing. The maximum yield of secreted endostatin during fermentation was 40 mg/liter. Up to 28 mg of endostatin was purified from 1 liter of cell culture broth. The biological activity of recombinant protein was tested in a bovine aortic endothelial (BAE) cell proliferation assay. The recombinant endostatin inhibited the growth of BAE cells stimulated by basic fibroblast growth factor, and its ED50 was comparable to that from a previous report. Flow cytometric measurements of BAE cells cultivated in medium with endostatin demonstrated a cell cycle arrest mainly in the G0/G1 phase and a decrease in the S phase.     

High-level expression and purification of a recombinant hBD-1 fused to LMM protein in Escherichia coli

In this work, we present the production of an active 43 aa recombinant human beta-defensin-1 (rhBD-1(43)) in Escherichia coli AD202 cells using specific pLMM1-rhBD-1 expression system. Unique solubility properties of the C-terminal fragment of light meromyosin (LMM) allowed us to overcome foreseeable problems with isolation procedures and toxicity caused by rhBD-1 to the host organism. As a result, the majority of fusion protein (LMM-rhBD-1(43)) was obtained in the soluble state, isolated by a low salt-high salt treatment of total cell protein. The rhBD-1(43) was cleaved from the fusion with Protease 4 and purified on CM Sepharose Fast Flow column with the yield of approximately 1 mg rhBD-1(43) from 6 g of wet weight cells. Purified rhBD-1(43) showed antimicrobial activity against E. coli ML-35p at a concentration of 129 microM. The procedure of rhBD-1 expression and purification we present can provide a reliable and simple method for production of different cationic peptides for biological studies.     

High-level recombinant protein production in bioreactors using the baculovirus-insect cell expression system

In order to develop an efficient process for large-scale production of recombinant protein, various factors were studied which affect the productivity of Sf-9 (Spodoptera frugiperda) insect cells when using the baculovirus expression system. It was shown that upon infection with the Bac-BRV6L recombinant baculovirus, the level per cell of VP6 (a bovine rotavirus nucleocapsid protein) would drop 10-fold when host cell density at the time of infection increased from 2 x 10(6) to 3 x 10(6) cells/mL. The decrease was found to be totally reversible by culture medium renewal after infection, even when cells were infected at the stationary phase. Recombinant protein production was 4-6 times higher using TNMFH medium supplemented with 10% fetal bovine serum (FBS) than in IPL/41 serum-free medium. Fine-tuning of infection parameters in a 4-L surface-aerated bioreactor resulted in the production of typically 350 mg/L of VP6 protein, representing more than 25% of total cell proteins.     

High-level expression of recombinant human soluble thrombomodulin in serum-free medium by CHO-K1 cells

Cultivation of gene-engineered Chinese hamster ovary (CHO-K1) cells that produce recombinant human soluble thrombomodulin (rsTM) was investigated to optimize conditions for high-level expression of the protein in a serum-free medium. For economic protein production, oxygenation of cultures with pure O₂ permitted sufficient cell growth for high rsTM production with only 1 g/l of microcarriers and a low foetal bovine serum concentration. A longer growth phase (over 5 days) with serum was important to establish sufficient growth of this cell line on the microcarriers for subsequent serum-free culture, and to support a long-term production phase (about 2 months). In the production phase, a high glucose concentration (6.15 g/l) in the serum-free medium was very effective for prolonging the harvest cycle interval. Under these conditions, up to 100 mg/l rsTM was expressed in the conditioned medium. The rates of glucose consumption (G) and lactae production (L) were measured periodically and their ratio (L/G ratio) correlated with rsTM productivity. When the average L/G ratio was lower, reflecting a lower lactate production rate due to appropriate oxygenation of the culture, the specific rsTM production rate increased. Thus it may be possible to estimate protein productivity from L/G ratios calculated from the glucose and lactate measurements. Correspondence to: M. Ogata     

Engineering a novel secretion signal for cross-host recombinant protein expression

Protein secretion is conferred by a hydrophobic secretion signal usually located at the N-terminal of the polypeptide. We report here, the identification of a novel secretion signal (SS) that is capable of directing the secretion of recombinant proteins from both prokaryotes and eukaryotes. Secretion of fusion reporter proteins was demonstrated in Escherichia coli, Saccharomyces cerevisiae and six different eukaryotic cells. Estrogen-inducibility and secretion of fusion reporter protein was demonstrated in six common eukaryotic cell lines. The rate of protein secretion is rapid and its expression profile closely reflects its intracellular concentration of mRNA. In bacteria and yeast, protein secretion directed by SS is dependent on the growth culture condition and rate of induction. This secretion signal allows a flexible strategy for the production and secretion of recombinant proteins in numerous hosts, and to conveniently and rapidly study protein expression.     

High-level production of Serratia proteamaculans metalloprotease using a recombinant ABC protein exporter-mediated secretion system in Pseudomonas fluorescens

Serratia proteamaculans metalloprotease (SPP) was successfully secreted by a heterologous ABC protein exporter, the Pseudomonas fluorescens TliDEF, in recombinant host strains. Escherichia coli and P. fluorescens cells containing the SPP-encoding gene showed the extracellular protease activity only when the TliDEF-encoding gene cluster was coexpressed. Recombinant P. fluorescens produced an approximately 34.8-fold higher amount of extracellular SPP than did E. coli. The use of a more nutrient-rich medium and controlled dissolved oxygen conditions was effective in increasing SPP secretion in P. fluorescens batch fermentation (an 8.7-fold increase from 41.8 U/mL to 365.2 U/mL). Therefore, SPP, which could not be secreted without an ABC protein exporter, was produced in large quantities by applying the heterologous TliDEF exporter in P. fluorescens. The results also suggest that the use of the ABC protein exporter in P. fluorescens could be an efficient production platform for an industrially promising type I secretion pathway-dependent enzyme.     

High-level soluble expression of hIGF-1 fusion protein in recombinant Escherichia coli

Human insulin-like growth factor 1 (hIGF-1) is one kind of growth factor with clinical significance in medicine. The expression of TrxA-hIGF-1 fusion protein was rationally compared in three different Escherichia coli hosts (BL21 (DE3), Rosetta (DE3) and Rosetta-gami (DE3)) with the transformation of plasmid pET32-hIGF-1. The highest productivity of soluble hIGF-1 fusion protein was achieved in E. coli Rosetta-gami (DE3). Moreover, the effects of different expression conditions in this E. coli Rosetta-gami (DE3)/pET32-hIGF-1 host were systematically investigated to improve the expression level of the fusion protein. Under the optimized conditions, a high percent of the target fusion protein (96%) was expressed as soluble form with the volumetric production of soluble fusion protein reaching up to 2.06 g/L. After cell disruption, the soluble fusion protein was separated effectively by affinity chromatography and cleaved by enterokinase, with the concentration of mature hIGF-1 reaching up to 0.42 g/L in the mixture. The present work should be useful for the enhanced production of soluble protein with multiple disulfide bonds in E. coli.     

Improved protein synthesis and secretion through medium enrichment in a stable recombinant yeast strain

Two Saccharomyces cerevisiae strains were employed to investigate the effects of medium enrichment on the expression and secretion of a recombinant protein. One was a stable autoselection strain with mutations in the ura3, fur1, and urid-k genes. The combination of these three mutations blocks both the pyrimidine nucleotide biosynthetic and salvage pathways and is lethal to the cells. Retention of the plasmid, which carries a URA3 gene, was essential for cell viability. Therefore, all media were selective, allowing cultivation of the strain in complex medium. The second strain was a nonautoselection (control) strain and is isogenic to the first except for the fur1 and urid-k mutations. The plasmid utilized contains the yeast invertase gene under the control of the MFalpha1 promoter and leader sequence. The expression and secretion of invertase for the autoselection strain were examined in batch culture for three media: a minimal medium (SD), a semidefined medium (SDC), and a rich complex medium (YPD). Biomass yields and invertase productivity (volumetric activity) increased with the complexity of the medium; total invertase volumetric activity in YPD was 100% higher than in SDC and 180% higher than in SD. Specific activity, however, was lowest in the SDC medium. Secretion efficiency was extremely high in all three media; for the majority of the culture, 80-90% of the invertase was secreted into the periplasmic space and/or culture medium. A glucose pulse at the end of batch culture in YPD facilitated the transport of residual cytoplasmic invertase. For the nonautoselection strain, invertase productivity did not improve as the medium was enriched from SDC to YPD, and plasmid stability in the complex YPD medium dropped from 54% to 34% during one batch fermentation. During long-term sequential batch culture in YPD, invertase activity decreased by 90% and the plasmid-containing fraction dropped from 56% to 8.8% over 44 generations of growth. The expression level for the autoselection strain, however, remained high and constant over this time period, and no reversion at the fur1 or urid-k locus was observed. (c) 1993 John Wiley & Sons, Inc.     

High-level expression of soluble recombinant RNase P protein from Escherichia coli.

We have expressed recombinant RNase P protein from Escherichia coli in high yield. A hexahistidine sequence at the amino terminus allowed protein purification in a single step. Mass spectrometry confirmed the molecular weight of the purified protein and indicated a purity of > 95%. Protein functionality was demonstrated by reconstitution of active holoenzyme.     

High-level expression and purification of biologically active recombinant pokeweed antiviral protein.

Pokeweed antiviral protein (PAP) from the leaves of the pokeweed plant, Phytolacca americana, is a naturally occurring single-chain ribosome-inactivating protein, which catalytically inactivates both prokaryotic and eukaryotic ribosomes. The therapeutic potential of PAP has gained considerable interest in recent years due to the clinical use of native PAP as the active moiety of immunoconjugates against cancer and AIDS. The clinical use of native PAP is limited due to inherent difficulties in obtaining sufficient quantities of a homogenously pure and active PAP preparation with minimal batch to batch variability from its natural source. Previous methods for expression of recombinant PAP in yeast, transgenic plants and Escherichia coli have resulted in either unacceptably low yields or were too toxic to the host system. Here, we report a successful strategy which allows high level expression of PAP as inclusion bodies in E. coli. Purification of refolded recombinant protein from solubilized inclusion bodies by size-exclusion chromatography yielded biologically active recombinant PAP (final yield: 10 to 12 mg/L). The ribosome depurinating in vitro N-glycosidase activity and cellular anti-HIV activity of recombinant PAP were comparable to those of the native PAP. This expression and purification system makes it possible to obtain sufficient quantities of biologically active and homogenous recombinant PAP sufficient to carry out advanced clinical trials. To our knowledge, this is the first large-scale expression and purification of biologically active recombinant PAP from E. coli.     

重组葡激酶基因在大肠杆菌内的高水平表达及生物学活性研究

将测序后的葡激酶重组质粒ＰＵＣ－ＳＡＫ经酶切后,组装于表达载体ｐＢＶ２２０,构建成ｐＢＶ－ＳＡＫ表达质粒,转化大肠杆菌。重组葡激酶表达水平达６０％～７０％,相对分子质量为 １５ ５００,主要以可溶状态存在于细胞中。生物活性测定证实,重组葡激酶具有很强的纤溶活性。     

High-level expression of the mycobacterial porin MspA in Escherichia coli and purification of the recombinant protein

MspA is the prototype of a new family of tetrameric porins and provides the main general diffusion pathway for hydrophilic compounds through the outer membrane of Mycobacterium smegmatis. Structural analysis was hampered by the scarce amount of pure protein. After replacement of the GC-rich codons of the mspA gene by codons optimal for high-level expression in Escherichia coli, the mature MspA protein was overproduced in E. coli. The recombinant MspA (rMspA) monomer (M(r) 20000) was purified by anion exchange and hydrophobic interaction chromatography yielding 2.6 mg pure protein per liter of culture. This exceeded the yield of the native protein 10-fold. Circular dichroism revealed that rMspA is folded in a native-like structure. rMspA assembled partially to the channel-forming tetramer both during expression in E. coli and after purification in vitro. Thus, overexpression in E. coli and chromatographic purification are key steps towards a high resolution structure of MspA.     

Excretion of human beta-endorphin into culture medium by using outer membrane protein F as a fusion partner in recombinant Escherichia coli

Escherichia coli BL21 strains were found to excrete a large amount of outer membrane protein F (OmpF) into culture medium during high-cell-density cultivation. From this interesting phenomenon, a novel and efficient OmpF fusion system was developed for the excretion of recombinant proteins by E. coli. The ompF gene of E. coli BL21(DE3) was first knocked out by using the red operon of bacteriophage lambda to construct E. coli MBEL-BL101. For the excretion of human beta-endorphin as a model protein, the beta-endorphin gene was fused to the C terminus of the E. coli ompF gene by using a linker containing the Factor Xa recognition site. To develop a fed-batch culture condition that allows efficient production of OmpF-beta-endorphin fusion protein, three different feeding strategies, an exponential feeding strategy and two pH-stat strategies with defined and complex nutrient feeding solutions, were examined. Among these, the pH-stat feeding strategy with the complex nutrient feeding solution resulted in the highest productivity (0.33 g of protein per liter per h). Under this condition, up to 5.6 g of OmpF-beta-endorphin fusion protein per liter was excreted into culture medium. The fusion protein was purified by anion-exchange chromatography and cleaved by Factor Xa to yield beta-endorphin, which was finally purified by reverse-phase chromatography. From 2.7 liters of culture supernatant, 545.4 mg of beta-endorphin was obtained.     

Addition of Co2+ to culture medium decides the functional expression of a recombinant nitrile hydratase in Escherichia coli

A nitrile hydratase (NHase) gene from Aurantimonas manganoxydans, cloned and expressed in Escherichia coli, gave an enzyme that efficiently hydrated 3-cyanopyridine to nicotinamide with high thermal stability. We have now found that adding Co²⁺ at 0.1 mM to LB medium was essential for production of an active enzyme. However, ≥0.3 mM Co²⁺ inhibited the growth of host cells in LB medium and decreased the production of the recombinant NHase. Furthermore, β-mercaptoethanol promoted regeneration of the Co²⁺-defective apoenzyme in vitro possibly by breaking a key disulfide bond thereby promoting the incorporation of Co²⁺ into the apoenzyme.     

Secretion of recombinant proteins into the culture medium by Escherichia coli and Staphylococcus aureus

The ability of staphylococcal protein A (SPA) to bind to the Fc part of IgG has been used for the purification of a number of heterologous gene products as fusion proteins. Both the SPA promoter and signal sequence function in Escherichia coli, as well as in a number of Gram-positive bacteria, which facilitates comparisons of the expressed specific products in different hosts. The expression system developed for E. coli yields excretion of the fusion protein to the growth medium, which makes E. coli a competitive alternative to Gram-positive bacteria for the expression of secreted products. The human peptide hormones insulin-like growth factors (IGF) I and II were expressed using the protein A system in E. coli and Staphylococcus aureus. Despite a high degree of structural homology, large differences in the yields were observed in the two hosts. This underlines the importance of investigating different bacterial hosts for a particular protein product.     

High-level expression of the Arabidopsis thaliana ethylene receptor protein ETR1 in Escherichia coli and purification of the recombinant protein

Ethylene responses in plants are mediated by a small family of membrane integral receptors including the ETR1 gene product which are similar to the two-component bacterial histidine kinase regulators. Detailed biochemical and structural analysis of the ethylene-receptor family was hampered by the scarce amount of pure protein. Here, we report the construction, expression, and single-step purification of the ETR1 receptor protein from Arabidopsis thaliana in a bacterial expression system. The DNA fragment encoding the mature ETR1 receptor protein was subcloned into the pET15b expression vector and highly expressed in derivatives C41(DE3) and C43(DE3) of the Escherichia coli strain BL21(DE3). The recombinant protein was solubilised from the bacterial cells using mild non-denaturing detergents and purified to homogeneity by Ni-NTA affinity chromatography, yielding approximately 2-3 mg pure protein per litre of cells. The molecular mass of the purified protein was estimated to be 78 kDa by SDS-PAGE. The expression and purification of recombinant ETR1 reported here provide a basis for detailed functional and structural studies of the receptor protein, which might help to understand signal perception and signal transduction of the phytohormone ethylene on the molecular level.