Proteome-based identification of fusion partner for high-level extracellular production of recombinant proteins in Escherichia coli

Extracellular production of recombinant proteins in Escherichia coli has several advantages over cytoplasmic or periplasmic production. However, nonpathogenic laboratory strains of E. coli generally excrete only trace amounts of proteins into the culture medium under normal growth conditions. Here we report a systematic proteome-based approach for developing a system for high-level extracellular production of recombinant proteins in E. coli. First, we analyzed the extracellular proteome of an E. coli B strain, BL21(DE3), to identify naturally excreted proteins, assuming that these proteins may serve as potential fusion partners for the production of recombinant proteins in the medium. Next, overexpression and excretion studies were performed for the 20 selected fusion partners with molecular weights below 40 kDa. Twelve of them were found to allow fused proteins to excrete into the medium at considerable levels. The most efficient excreting fusion partner, OsmY, was used as a carrier protein to excrete heterologous proteins into the medium. E. coli alkaline phosphatase, Bacillus subtilis alpha-amylase, and human leptin used as model proteins could all be excreted into the medium at concentrations ranging from 5 to 64 mg/L during the flask cultivation. When only the signal peptide or the mature part of OsmY was used as a fusion partner, no such excretion was observed; this confirmed that these proteins were truly excreted rather than released by outer membrane leakage. The recombinant protein of interest could be recovered by cleaving off the fusion partner by enterokinase as demonstrated for alkaline phosphatase as an example. High cell density cultivation allowed production of these proteins to the levels of 250-700 mg/L in the culture medium, suggesting the good potential of this approach for the excretory production of recombinant proteins.     

Development of a full‐length human protein production pipeline

There are many proteomic applications that require large collections of purified protein, but parallel production of large numbers of different proteins remains a very challenging task. To help meet the needs of the scientific community, we have developed a human protein production pipeline. Using high‐throughput (HT) methods, we transferred the genes of 31 full‐length proteins into three expression vectors, and expressed the collection as N‐terminal HaloTag fusion proteins in Escherichia coli and two commercial cell‐free (CF) systems, wheat germ extract (WGE) and HeLa cell extract (HCE). Expression was assessed by labeling the fusion proteins specifically and covalently with a fluorescent HaloTag ligand and detecting its fluorescence on a LabChip^® GX microfluidic capillary gel electrophoresis instrument. This automated, HT assay provided both qualitative and quantitative assessment of recombinant protein. E. coli was only capable of expressing 20% of the test collection in the supernatant fraction with ≥20 μg yields, whereas CF systems had ≥83% success rates. We purified expressed proteins using an automated HaloTag purification method. We purified 20, 33, and 42% of the test collection from E. coli, WGE, and HCE, respectively, with yields ≥1 μg and ≥90% purity. Based on these observations, we have developed a triage strategy for producing full‐length human proteins in these three expression systems.     

Incompatibility of outer membrane proteins OmpA and OmpF of Escherichia coli with secretion in Bacillus subtilis: Fusions with secretable peptides

The secretion of the outer membrane proteins OmpA and OmpF of Escherichia coli has previously been found to be blocked at an early intracellular step, when these proteins were fused to a bacillar signal sequence and expressed in Bacillus subtilis. We have now fused these proteins to long secretable polypeptides, the amino-terminal portions of alpha-amylase or beta-lactamase. In spite of this, no secretion of the fusion proteins was detected in B. subtilis. With the exception of a small fraction of the beta-lactamase fusion, the proteins were cell-bound with uncleaved signal sequences. Protease accessibility indicated that the fusion proteins were not even partially exposed on the outer surface of the cytoplasmic membrane. Thus there was no change of the location compared to the OmpA or OmpF fused to the signal sequence only. We conclude that, like OmpA and OmpF, the fusion proteins fold into an export-incompatible conformation in B. subtilis before the start of translocation, which we postulate to be a late post-translational event.     

大肠杆菌副产物合成途径删除提高外源蛋白表达水平

大肠杆菌是应用最广泛的外源基因表达宿主。为探索阻断副产物产生途径对提高大肠杆菌表达外源蛋白的能力,本实验以野生型大肠杆菌菌株为基础,删除其乳酸脱氢酶基因(ldhA),磷酸烯醇式丙酮酸合成酶基因(pps)和丙酮酸甲酸裂解酶基因(pflB)。在此基础上,以甘露聚糖酶基因man为报告基因,考察阻断以上代谢途径对大肠杆菌产酶能力的影响。结果显示,以上述三个基因叠加删除的三重突变株为宿主时,重组茵产酶水平最高,比酶活达到158.3 U/mg,相比野生出发菌株提高82.3%。     

Construction of hypervesiculation Escherichia coli strains and application for secretory protein production

Outer membrane vesicles (OMVs) are extracellular vesicles released from the surface of Gram-negative bacteria, including Escherichia coli. Several gene-deficient mutants relating to envelope stress (nlpI and degP) and phospholipid accumulation in the outer leaflet of the outer membrane (mlaA and mlaE) increase OMV production. This study examined the combinatorial deletion of these genes in E. coli and its effect on OMV production. The nlpI and mlaE double-gene-knockout mutant (ΔmlaEΔnlpI) showed the highest OMV production. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis-based quantitative analysis showed that OMV production by strain ΔmlaEΔnlpI was ~30 times that by the wild-type (WT). In addition, to evaluate the protein secretion capacity of OMVs, a green fluorescent protein (GFP) fused with outer membrane protein W (OmpW) was expressed in OMVs. Western blot analysis showed that GFP secretion through OMVs reached 3.3 mg/L in the culture medium of strain ΔmlaEΔnlpI/gfp, 500 times that for the WT. Our approach using OMVs for extracellular protein secretion in E. coli is an entirely new concept compared with existing secretion systems.     

Practical protocols for production of very high yields of recombinant proteins using Escherichia coli

The gram‐negative bacterium Escherichia coli offers a mean for rapid, high yield, and economical production of recombinant proteins. However, high‐level production of functional eukaryotic proteins in E. coli may not be a routine matter, sometimes it is quite challenging. Techniques to optimize heterologous protein overproduction in E. coli have been explored for host strain selection, plasmid copy numbers, promoter selection, mRNA stability, and codon usage, significantly enhancing the yields of the foreign eukaryotic proteins. We have been working on optimizations of bacterial expression conditions and media with a focus on achieving very high cell density for high‐level production of eukaryotic proteins. Two high‐cell‐density bacterial expression methods have been explored, including an autoinduction introduced by Studier (Protein Expr Purif 2005;41:207–234) recently and a high‐cell‐density IPTG‐induction method described in this study, to achieve a cell‐density OD₆₀₀ of 10–20 in the normal laboratory setting using a regular incubator shaker. Several practical protocols have been implemented with these high‐cell‐density expression methods to ensure a very high yield of recombinant protein production. With our methods and protocols, we routinely obtain 14–25 mg of NMR triple‐labeled proteins and 17–34 mg of unlabeled proteins from a 50‐mL cell culture for all seven proteins we tested. Such a high protein yield used the same DNA constructs, bacterial strains, and a regular incubator shaker and no fermentor is necessary. More importantly, these methods allow us to consistently obtain such a high yield of recombinant proteins using E. coli expression.     

Plant cell packs: a scalable platform for recombinant protein production and metabolic engineering

Industrial plant biotechnology applications include the production of sustainable fuels, complex metabolites and recombinant proteins, but process development can be impaired by a lack of reliable and scalable screening methods. Here, we describe a rapid and versatile expression system which involves the infusion of Agrobacterium tumefaciens into three‐dimensional, porous plant cell aggregates deprived of cultivation medium, which we have termed plant cell packs (PCPs). This approach is compatible with different plant species such as Nicotiana tabacum BY2, Nicotiana benthamiana or Daucus carota and 10‐times more effective than transient expression in liquid plant cell culture. We found that the expression of several proteins was similar in PCPs and intact plants, for example, 47 and 55 mg/kg for antibody 2G12 expressed in BY2 PCPs and N. tabacum plants respectively. Additionally, the expression of specific enzymes can either increase the content of natural plant metabolites or be used to synthesize novel small molecules in the PCPs. The PCP method is currently scalable from a microtiter plate format suitable for high‐throughput screening to 150‐mL columns suitable for initial product preparation. It therefore combined the speed of transient expression in plants with the throughput of microbial screening systems. Plant cell packs therefore provide a convenient new platform for synthetic biology approaches, metabolic engineering and conventional recombinant protein expression techniques that require the multiplex analysis of several dozen up to hundreds of constructs for efficient product and process development.     

Enhancing extracellular protein production in Escherichia coli by deleting the d‐alanyl‐d‐alanine carboxypeptidase gene dacC

d ‐Alanyl‐d ‐alanine carboxypeptidase DacC is important for synthesis and stabilization of the peptidoglycan layer of Escherichia coli. In this work, dacC of E. coli BL21 (DE3) was successfully deleted, and the effects of this deletion on extracellular protein production in E. coli were investigated. The extracellular activities and fluorescence value of recombinant amylase, green fluorescent protein, and α‐galactosidase of the deletion mutants were increased by 82.3, 29.1, and 37.7%, respectively, compared with that of control cells. The outer membrane permeability and intracellular soluble peptidoglycan accumulation of deletion mutant were also enhanced compared with those of control cells, respectively. Based on fluorescence‐assisted cell sorting analyses, we found that the morphology of the E. coli deletion mutant cells was altered compared with that of control cells. Local transparent bulges in the poles of the E. coli mutant with deletion of the dacC gene were found by transmission electron microscopy analysis. These bulges in the poles could explain the improvement in the production of extracellular protein by the E. coli mutant with deletion of the dacC gene. These findings provide important insights into the extracellular production of proteins using E. coli as microbial cell factories.     

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.     

Twenty-four-well plate miniature bioreactor high-throughput system: assessment for microbial cultivations

High-throughput (HT) miniature bioreactor (MBR) systems are becoming increasingly important to rapidly perform clonal selection, strain improvement screening, and culture media and process optimization. This study documents the initial assessment of a 24-well plate MBR system, Micro (micro)-24, for Saccharomyces cerevisiae, Escherichia coli, and Pichia pastoris cultivations. MBR batch cultivations for S. cerevisiae demonstrated comparable growth to a 20-L stirred tank bioreactor fermentation by off-line metabolite and biomass analyses. High inter-well reproducibility was observed for process parameters such as on-line temperature, pH and dissolved oxygen. E. coli and P. pastoris strains were also tested in this MBR system under conditions of rapidly increasing oxygen uptake rates (OUR) and at high cell densities, thus requiring the utilization of gas blending for dissolved oxygen and pH control. The E. coli batch fermentations challenged the dissolved oxygen and pH control loop as demonstrated by process excursions below the control set-point during the exponential growth phase on dextrose. For P. pastoris fermentations, the micro-24 was capable of controlling dissolved oxygen, pH, and temperature under batch and fed-batch conditions with subsequent substrate shot feeds and supported biomass levels of 278 g/L wet cell weight (wcw). The average oxygen mass transfer coefficient per non-sparged well were measured at 32.6 +/- 2.4, 46.5 +/- 4.6, 51.6 +/- 3.7, and 56.1 +/- 1.6 h(-1) at the operating conditions of 500, 600, 700, and 800 rpm shaking speed, respectively. The mixing times measured for the agitation settings 500 and 800 rpm were below 5 and 1 s, respectively.     

New tools for recombinant protein production in Escherichia coli: A 5‐year update

The production of proteins in sufficient amounts is key for their study or use as biotherapeutic agents. Escherichia coli is the host of choice for recombinant protein production given its fast growth, easy manipulation, and cost‐effectiveness. As such, its protein production capabilities are continuously being improved. Also, the associated tools (such as plasmids and cultivation conditions) are subject of ongoing research to optimize product yield. In this work, we review the latest advances in recombinant protein production in E. coli.     

A bacterial expression system revisited for the recombinant production of cystine-rich plant lipid transfer proteins

Non-specific lipid transfer proteins (nsLTPs) are abundant and ubiquitous cystine-rich proteins that are capable, in vitro, of binding lipids and hydrophobic molecules. In view to probe the lipid binding properties of the wheat nsLTP1, mutant variants may represent a powerful tool. To this end, a synthetic gene, encoding a mature wheat nsLTP1 polypeptide, was designed to ensure high level expression in Escherichia coli. The bacterial expression host strain, a translational fusion strategy, and convenient cleavage and purification procedures were optimized to produce in standard fermentation conditions, a significant amount (15 mg/L final yield), of a soluble and correctly folded recombinant nsLTP1. This highly amenable expression system is helpful in order to investigate structure-activity relationships of plant nsLTP.     

Microbial production of amino acid-modified spider dragline silk protein with intensively improved mechanical properties

Spider dragline silk is a remarkably strong fiber with impressive mechanical properties, which were thought to result from the specific structures of the underlying proteins and their molecular size. In this study, silk protein 11R26 from the dragline silk protein of Nephila clavipes was used to analyze the potential effects of the special amino acids on the function of 11R26. Three protein derivatives, ZF4, ZF5, and ZF6, were obtained by site-directed mutagenesis, based on the sequence of 11R26, and among these derivatives, serine was replaced with cysteine, isoleucine, and arginine, respectively. After these were expressed and purified, the mechanical performance of the fibers derived from the four proteins was tested. Both hardness and average elastic modulus of ZF4 fiber increased 2.2 times compared with those of 11R26. The number of disulfide bonds in ZF4 protein was 4.67 times that of 11R26, which implied that disulfide bonds outside the poly-Ala region affect the mechanical properties of spider silk more efficiently. The results indicated that the mechanical performances of spider silk proteins with small molecular size can be enhanced by modification of the amino acids residues. Our research not only has shown the feasibility of large-scale production of spider silk proteins but also provides valuable information for protein rational design.     

优化培养条件和裂解方法提高hRANKL在大肠杆菌内的表达

RANKL/RANK/OPG轴在骨代谢过程中起到中心调节作用,也是近年来骨相关疾病治疗研究的热点之一。RANKL蛋白在RANKL/RANK/OPG轴信号传递过程中起到关键作用,在骨代谢相关实验研究中用途广泛。但是,使用大肠杆菌Escherichia coli可溶表达重组人源RANKL蛋白 (hRANKL) 时产量远低于鼠源RANKL (mRANKL)。本研究通过将LB培养基pH值调整并稳定在7.5、降低诱导表达温度至16 ℃并优化细菌裂解条件,成功地将可溶hRANKL产量增加到了对照组的5?12倍。该方法有效提高了hRANKL在大肠杆菌中可溶表达的产量,同时也是研究重组蛋白在大肠杆菌内的可溶表达策略的有益尝试。     

Simple production of resilin-like protein hydrogels using the Brevibacillus secretory expression system and column-free purification

Resilin, an insect structural protein, has excellent flexibility, photocrosslinking properties, and temperature responsiveness. Recombinant resilin-like proteins (RLPs) can be fabricated into three-dimensional (3D) structures for use as cell culture substrates and highly elastic materials. A simplified, high-yielding production process for RLPs is required for their widespread application. This study proposes a simple production process combining extracellular expression using Brevibacillus choshinensis (B. choshinensis) and rapid column-free purification. Extracellular production was tested using four representative signal peptides; B. choshinensis was found to efficiently secrete Rec1, an RLP derived from Drosophila melanogaster, regardless of the type of signal peptide. However, it was suggested that Rec1 is altered by an increase in the pH of the culture medium associated with prolonged incubation. Production in a jar fermentor with controllable pH yielded 530 mg Rec1 per liter of culture medium, which is superior to productivity using other hosts. The secreted Rec1 was purified from the culture supernatant via (NH₄)₂SO₄ and ethanol precipitations, and the purified Rec1 was applied to ring-shaped 3D hydrogels. These results indicate that the combination of secretory production using B. choshinensis and column-free purification can accelerate the further application of RLPs.     

The pathogenicity of Aeromonas strains relative to genospecies and phenospecies identification

A high yield of Escherichia coli outer membrane proteins OmpA (about 200 mg/l) and OmpF (about 100 mg/l) was obtained in Bacillus subtilis when produced intracellularly. The yield was more than 100-fold higher than the yield of these proteins by a similar vector containing the complete signal sequence of alpha-amylase of B. amyloliquefaciens. Both proteins isolated after breakage of the B. subtilis cells by low-speed centrifugation were about 70% pure and could be solubilized by Sarkosyl, SDS and guanidine hydrochloride.     

High‐throughput instant quantification of protein expression and purity based on photoactive yellow protein turn off/on label

Quantifying the concentration and purity of a target protein is essential for high‐throughput protein expression test and rapid screening of highly soluble proteins. However, conventional methods such as PAGE and dot blot assay generally involve multiple time‐consuming tasks requiring hours or do not allow instant quantification. Here, we demonstrate a new method based on the Photoactive yellow protein turn Off/On Label (POOL) system that can instantly quantify the concentration and purity of a target protein. The main idea of POOL is to use Photoactive Yellow Protein (PYP), or its miniaturized version, as a fusion partner of the target protein. The characteristic blue light absorption and the consequent yellow color of PYP is absent when initially expressed without its chromophore, but can be turned on by binding its chromophore, p‐coumaric acid. The appearance of yellow color upon adding a precursor of chromophore to the co‐expressed PYP can be used to check the expression amount of the target protein via visual inspection within a few seconds as well as to quantify its concentration and purity with the aid of a spectrometer within a few minutes. The concentrations measured by the POOL method, which usually takes a few minutes, show excellent agreement with those by the BCA Kit, which usually takes ～1 h. We demonstrate the applicability of POOL in E. coli, insect, and mammalian cells, and for high‐throughput protein expression screening.     

Optimized procedure for renaturation of recombinant human bone morphogenetic protein-2 at high protein concentration

The human gene encoding the mature form of bone morphogenetic protein-2 (hBMP-2), a dimeric disulfide-bonded protein of the cystine knot growth factor family, was expressed in recombinant Escherichia coli using a temperature-inducible expression system. The recombinant protein was produced in the form of cytoplasmic inclusion bodies and the effect of different variables on the renaturation of rhBMP-2 was investigated. In particular, variables such as pH, redox conditions, protein concentration, temperature, the presence of different types of aggregation suppressors, and host cell contaminants were studied with respect to their effect on aggregation during refolding and on the final renaturation yield of rhBMP-2. It is shown that the renaturation yield is particularly sensitive to pH, temperature, protein concentration, and the presence of aggregation suppressors. In contrast, little effect of the redox conditions and the ionic strength on the renaturation yield was observed, as equal yields were obtained in a broad range of reduced to oxidized glutathione ratios and concentrations of NaCl, respectively. The aggregation suppressor 2-(cyclohexylamino)ethanesulfonic acid (CHES) proved to be superior with respect to the final renaturation yield, although, in comparison to the more common arginine, it was less efficient in preventing aggregation of rhBMP-2 during refolding. Detergent washing of inclusion bodies was sufficient, as further purification of rhBMP-2 prior to refolding was without effect on the final renaturation yield. An increase in the concentration of renatured rhBMP-2 was achieved by a pulsed refolding procedure by which up to a total amount of 2.1 mg mL(-1) rhBMP-2 could be transferred in seven pulses into the renaturation buffer with an overall refolding yield of 38%, corresponding to 0.8 mg mL(-1) renatured dimeric rhBMP-2. Furthermore, a simplified purification procedure is presented that also includes freeze-drying for long-term storage of biologically active rhBMP-2. Finally, it is shown that the appearance of rhBMP-2 variants could be avoided by using a host strain overexpressing rare codon tRNAs.