Improving Fab’ fragment retention in an autonucleolytic <Emphasis Type="Italic">Escherichia coli</Emphasis> strain by swapping periplasmic nuclease translocation signal from OmpA to DsbA

Objectives

To reduce unwanted Fab’ leakage from an autonucleolytic Escherichia coli strain, which co-expresses OmpA-signalled Staphylococcal nuclease and Fab’ fragment in the periplasm, by substituting in Serratial nuclease and the DsbA periplasm translocation signal as alternatives.

Results

We attempted to genetically fuse a nuclease from Serratia marcescens to the OmpA signal peptide but plasmid construction failed, possibly due to toxicity of the resultant nuclease. Combining Serratial nuclease to the DsbA signal peptide was successful. The strain co-expressing this nuclease and periplasmic Fab’ grew in complex media and exhibited nuclease activity detectable by DNAse agar plate but its growth in defined medium was retarded. Fab’ coexpression with Staphylococcal nuclease fused to the DsbA signal peptide resulted in cells exhibiting nuclease activity and growth in defined medium. In cultivation to high cell density in a 5 l bioreactor, DsbA-fused Staphylococcal nuclease co-expression coincided with reduced Fab’ leakage relative to the original autonucleolytic Fab’ strain with OmpA-fused staphylococcal nuclease.

Conclusions

We successfully rescued Fab’ leakage back to acceptable levels and established a basis for future investigation of the linkage between periplasmic nuclease expression and leakage of co-expressed periplasmic Fab’ fragment to the surrounding growth media.

     

Development of a high yielding E. coli periplasmic expression system for the production of humanized Fab' fragments

Humanized Fab′ fragments may be produced in the periplasm of Escherichia coli but can be subject to degradation by host cell proteases. In order to increase Fab′ yield and reduce proteolysis we developed periplasmic protease deficient strains of E. coli. These strains lacked the protease activity of Tsp, protease III and DegP. High cell density fermentations indicated Tsp deficient strains increased productivity two fold but this increase was accompanied by premature cell lysis soon after the induction of Fab′ expression. To overcome the reduction in cell viability we introduced suppressor mutations into the spr gene. The mutations partially restored the wild type phenotype of the cells. Furthermore, we coexpressed a range of periplasmic chaperone proteins with the Fab′, DsbC had the most significant impact, increasing humanized Fab′ production during high cell density fermentation. When DsbC coexpression was combined with a Tsp deficient spr strain we observed an increase in yield and essentially restored “wild type” cell viability. We achieved a final periplasmic yield of over 2.4g/L (final cell density OD₆₀₀ 105), 40 h post Fab′ induction with minimal cell lysis.The data suggests that proteolysis, periplasm integrity, protein folding and disulphide bond formation are all potential limiting steps in the production of Fab′ fragments in the periplasm of E. coli. In this body of work, we have addressed these limiting steps by utilizing stabilized protease deficient strains and chaperone coexpression. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 33:212–220, 2017     

Temperature-regulated expression of the tac/lacI system for overproduction of a fungal xylanase in Escherichia coli

 Temperature-regulated expression of recombinant proteins in the tac promoter (P_tac) system was investigated. Expression levels of fungal xylanase and cellulase from N. patriciarum in E. coli strains containing the natural lacI gene under the control of the P_tac markedly increased with increasing cultivation temperature in the absence of a chemical inducer. The specific activities (units per milligram protein of crude enzyme) of the fungal xylanase and cellulase produced from recombinant E. coli strain pop2136 grown at 42°C were about 4.5 times higher than those of the cells grown at 23°C and were even slightly higher when compared with cells grown in the presence of the inducer isopropyl β-D-thiogalactopyranoside. The xylanase expression level in the temperature-regulated P_tac system was about 35% of total cellular protein. However, this system can not be applied to E. coli strains containing lacI ^q, which confers over production of the lac repressor, for high-level expression of recombinant proteins. In comparison with the λP_L system, the P_tac-based xylanase plasmid in E. coli pop2136 gave a considerably higher specific activity of the xylanase than did the best λP_L-based construct using the same thermal induction procedure. The high-level expression of the xylanase using the temperature-regulated P_tac system was also obtained in 10-litre fermentation studies using a fed-batch process. These results unambiguously demonstrated that the temperature-modulated P_tac system can be used for overproduction of some non-toxic recombinant proteins. Received: 27 June 1995/Received revision: 13 September 1995/Accepted: 30 September 1995     

High-level production and secretion of a mouse-human chimeric Fab fragment with specificity to human carcino embryonic antigen in Escherichia coli

A high-level secretion system for the production of mouse-human chimeric antibody 21B2 (MHC 21B2) Fab fragment specific for human carcino embryonic antigen (hCEA) in Escherichia coli has been constructed. The genes encoding a light chain and an Fd fragment (a variable region and the CH₁ domain of a heavy chain) of a mouse-human chimeric antibody were directly fused to the signal peptide of the E. coli ompF gene sequence. E. coli cells containing expression vectors in which each of the two genes are located downstream of a separate tac promoter were able to secrete the light chain and Fd fragment as two of their major cellular proteins. The signal peptides were efficiently removed from the primary products by post-translational processing, although they formed insoluble aggregates, possibly in the periplasm. In high-cell-density culture experiments using a jar fermentor, the amount of light chain and Fd fragment produced was at levels of up to 2.88 g/l and 1.28 g/l culture, respectively. By optimizing the conditions that encourage correct folding, formation of disulphide bonds, and association of the light chain with the Fd fragment, we have established a procedure that can purify, refold, and combine aggregated products to electrophoretically homogeneous Fab fragment with a yield of approximately 47%. Fab fragment produced in this manner shows essentially the same antigen-binding activity and specificity to hCEA as the parental mouse antibody 21B2 (MoAb 21B2). Correspondence to: T. Shibui     

Secretion of a functional Fab fragment in Escherichia coli and the influence of culture conditions

Summary Genes encoding a light chain and an Fd region (a variable region and a CH1 domain of a heavy chain) of a mouse-human chimeric antibody with specificity for human carcinoembryonic antigen (CEA) were fused to a DNA segment coding for the signal peptide of Escherichia coli ompF. E. coli cells harbouring an expression vector containing these genes downstream of a tac promoter were able to secrete a Fab fragment of the antibody efficiently. When the cells were cultured at 37° C and the inducer (isopropyl-\-d-thiogalactopyranoside, IPTG) concentration was 1 mm (standard conditions), production of functional Fab was very low (medium; 200 ng/l culture and periplasm; <90 ng/l culture). In order to optimize functional Fab production, we examined the influence of culture conditions (i.e. temperature and the inducer concentration) on secretion of the product. It was found that a 12.7-fold higher amount of Fab fragment could be produced at 30° C using 0.1 mm IPTG, as compared with standard conditions. Under these optimal conditions, functional Fab accumulated in the periplasm and culture medium for 10 h after induction and the total production level was found to reach approximately 4.5 mg/l culture. Correspondence to: T. Shibui     

Construction of recombinant K88 DNA with Ptac promoter

The gene encoding K88ab was localized on the 11.6 kbHindIII-HindIII fragment of 74 kb plasmid DNA ofE. coli 7301. The smallest recombinant DNA producing the K88ab antigen was obtained by excision of the 5.15 kbEcoRI-EcoRI fragment from recombinant DNA composed of the 11.6 kb K88ab fragment in the pBR322 vectro. The size of the smallest fragment was 6.5 kb. Expression of the K88ab antigen was controlled by the P1 promoter of the pBR322 vector. Substitution of promoter P_tac for promoter P1 made it possible to achieve expression of the K88ab antigen byE. coli MT. Substitution of promoter P_L for promoter P1 failed to achieve expression of the K88 ab antigen in the recipient strains used.     

Fermenter production of an artificial fab fragment,rationally designed for the antigen cystatin,and its optimized crystallization through constant domain shuffling

The synthetic antibody model “M41” was rationally designed with a binding site complementary to chicken egg white cystatin as the prescribed antigen. In order to permit comparison between the computer model and an experimental three-dimensional structure of the artificial protein, its X-ray crystallographic analysis was pursued. For this purpose, M41 was expressed as a recombinant Fab fragment in E. coli by medium cell density fermentation employing the tightly regulated tetracycline promoter. The Fab fragment was efficiently purified via a His-6 tail fused to its heavy chain and immobilized metal affinity chromatography. To raise the chances for the productive formation of crystal packing contacts, three versions of the Fab fragment were generated with differing constant domains. One of these, the variant with murine C_K and C_H 1_γ1 domains, was successfully crystallized by microseeding in a sitting drop. The orthorhombic crystals exhibited symmetry of the space group P2₁2₁2₁ with unit cell dimensions a = 104.7 Å, b = 113.9 Å, c = 98.8 Å and diffracted X-rays to a nominal resolution of 2.5 Å. © 1995 Wiley-Liss, Inc.     

Evaluation of promoters for gene expression in polyhydroxyalkanoate-producing Cupriavidus necator H16

Five kinds of promoters were evaluated as tools for regulated gene expression in the PHA-producing bacterium Cupriavidus necator. Several broad-host-range expression vectors were constructed by which expression of a reporter gene gfp was controlled by P _lac , P _tac , or P _BAD derived from Escherichia coli, or promoter regions of phaC1 (P _phaC ) or phaP1 (P _phaP ) derived from C. necator. Then, the gfp-expression profiles were determined in C. necator strains harboring the constructed vectors when the cells were grown on fructose or soybean oil. P _lac , P _tac , P _phaC , and P _phaP mediated constitutive gene expression, among which P _tac was the strongest promoter. lacI-P _tac was not thoroughly functional even after addition of isopropyl-β-d-thiogalactopyranoside (IPTG), probably due to inability of C. necator to uptake IPTG. Gene expression by araC-P _BAD could be regulated by varying l-arabinose concentration in the medium, although P(3HB) production rate was slightly decreased in the recombinant. phaR-P _phaP exhibited an expression profile tightly coupled with P(3HB) accumulation, suggesting application of the vector harboring phaR-P _phaP for gene expression specific at the PHA-biosynthesis phase. The properties of these promoters were expected to be useful for effective engineering of PHA biosynthesis in C. necator.     

The striking effects of spacer and terminator sequences on the synthesis of porcine growth hormone inEscherichia coli

Summary Two types of expression vectors containing theP _tac orP _L promoters, synthetic ribosomalbinding sequences (RBS), and a transciptional terminator (rrnBT₁T₂) were constructed for the production of porcine growth hormone (pGH) inEscherichia coli. The results demonstrated that the nucleotide sequence between the RBS and the start codon, ATG, was critical for the yields of pGH. The rrnBT₁T₂ terminator was essential for the efficient expression ofpGH in theP _tac -driven vectors, but reduced the synthesis of pGH in theP _L -vectors. A leaky repression was observed in the JM103 cells containing theP _tac -plasmids.     

Recombinant anti-stefin A Fab fragment: sequence analysis of the variable region and expression in Escherichia coli

Human stefin A is an inhibitor of lysosomal cysteine proteinases cathepsin B, H, L and S. In the present report we describe the cloning and expression of anti-stefin A Fab fragment A22 in E. coli. We have determined the nucleotide sequences of the antibody heavy and light chain and compared them to the murine immunoglobulin germ line sequences. Expression of the two antibody chains was achieved using a single vector with a PhoA promoter and coding regions placed after the signal sequences, directing them to the periplasmic space. The A22 Fab fragment was extracted from the periplasmic space and expression was confirmed by Western blot analysis. The recombinant A22 Fab fragment had an affinity for stefin A comparable to the original monoclonal antibody, as determined by ELISA.     

Production characteristics of interferon-α using an l-arabinose promoter system in a high-cell-density culture

 Using high-cell-density culture of Escherichia coli under the control of an l-arabinose promoter (P_araB), several factors affecting the production of recombinant protein and the formation of inclusion bodies were studied. The inducer, l-arabinose, showed a maximal induction level above 10.7 mM in the final concentration. The concentration of inducer also affected the partition of interferon-α (IFN-α) into the soluble form and inclusion bodies. Induction kinetics of the rate of accumulation of IFN-α on the P_araB promoter showed a slower rate than those of other promoter systems, for example T7, lac or tac. These innate characteristics of P_araB enabled cells to grow continuously in spite of the metabolic burden induced by the expression of foreign protein. The duration time of induction could control the expression of both soluble and insoluble protein. The ratio of yeast extract to glycerol (N/C ratio) in feeding media significantly affected both the production level of recombinant protein and inclusion body formation. The reason for decreasing specific bioactivity during induction can be explained by the increased proportion of inclusion bodies in the total expressed IFN-α. Received: 21 May 1999 / Received last revision: 16 August 1999 / Accepted: 2 September 1999     

Versatile Escherichia coli Expression Vectors for Production of Truncated Proteins

Several expression vector plasmids containing the tac promoter, the rrnBT₁T₂ terminator, and the pUC ori sequence were constructed. Some of them, the pES series, have a start codon in all three reading frames and multiple cloning sites downstream of the tac promoter and have stop codons also in all three frames and additional stop codons accompanying restriction sites. They are designed for versatile expression of truncated proteins which are produced by deleting portions of the inserted DNA.     

Requirements for the high-level expression of murine interleukin-3 cDNA inEscherichia coli

Summary Murine interleukin-3 (Mu IL-3) cDNA was previously expressed inEscherichia coli using atac promoter and a constitutive high copy number plasmid vector. We found that significant increases in expression levels could be realized by using thetac promoter for the expression of Mu IL-3 in a plasmid vector possessing a temperature-inducible runaway-replicon. In contrast, use of anlpp promoter under similar conditions did not result in an increase in the Mu IL-3 expression level. Significant differences were observed when the expression levels of IL-3 were monitored in variousE. coli hosts having different genetic backgrounds. A mutant ofE. coli which lacks the protease La was found to increase the level of IL-3 produced. This report describes the effect of a specific protease-deficientE. coli host strain, as well as the effect of different promoters and plasmid replicons on the expression levels and stability of a heterologous gene product.     

丙酮酸和乙酰-CoA协同促进L-亮氨酸的合成

【目的】通过理性改造柠檬酸合酶(citrate synthase,CS)、丙酮酸脱氢酶系E1p (pyruvate dehydrogenase complex,PDHC,编码基因aceE)和ATP-柠檬酸裂解酶(ATP-Citrate lyase,ACL),有效供应胞内丙酮酸和乙酰-CoA,以提高L-亮氨酸产量。【方法】以谷氨酸棒杆菌(Corynebacterium glutamicum)为底盘细胞,分析不同CS和PDHC酶活水平对L-亮氨酸合成的影响。随后,考查协同改造CS和PDHC或引入绿硫菌(Chlorobium tepidum)中ACL对L-亮氨酸合成的影响。【结果】低强度的CS酶活(即重组菌XL-3 P_(dapA-R2)gltA)有利于L-亮氨酸的合成,L-亮氨酸产量达到17.5±0.6 g/L。而改变PDHC酶活水平不利于L-亮氨酸的合成。此外,以启动子P_(dapA-R2)控制CS表达,而以启动子P_(gapA)控制PDHC表达时(即重组菌XL-4),可实现胞内丙酮酸和乙酰-CoA的有效供给,L-亮氨酸产量达到20.2±1.7 g/L,且显著降低副产物产量。若在重组菌XL-4中引入C.tepidum,ACL会显著抑制菌体生长而不利于L-亮氨酸合成,而引入到出发菌XL-3中因胞内丙酮酸和乙酰-CoA得到有效供给,目标重组菌XL-5L-亮氨酸产量达到18.5±1.2 g/L,比出发菌株XL-3增加了14.2%。【结论】重组菌XL-4中因协同控制CS和PDHC酶活,从而实现胞内丙酮酸和乙酰-CoA有效供给,促进L-亮氨酸的合成。该研究结果对后续利用代谢工程技术强化微生物合成L-亮氨酸等支链氨基酸具有重要的参考价值。     

Employment of a Promoter-Swapping Technique Shows that PhoU Modulates the Activity of the PstSCAB2 ABC Transporter in Escherichia coli

Expression of the Pho regulon in Escherichia coli is induced in response to low levels of environmental phosphate (P_i). Under these conditions, the high-affinity PstSCAB₂ protein (i.e., with two PstB proteins) is the primary P_i transporter. Expression from the pstSCAB-phoU operon is regulated by the PhoB/PhoR two-component regulatory system. PhoU is a negative regulator of the Pho regulon; however, the mechanism by which PhoU accomplishes this is currently unknown. Genetic studies of phoU have proven to be difficult because deletion of the phoU gene leads to a severe growth defect and creates strong selection for compensatory mutations resulting in confounding data. To overcome the instability of phoU deletions, we employed a promoter-swapping technique that places expression of the phoBR two-component system under control of the P_tac promoter and the lacO^ID regulatory module. This technique may be generally applicable for controlling expression of other chromosomal genes in E. coli. Here we utilized P_phoB::P_tac and P_pstS::P_tac strains to characterize phenotypes resulting from various ΔphoU mutations. Our results indicate that PhoU controls the activity of the PstSCAB₂ transporter, as well as its abundance within the cell. In addition, we used the P_phoB::P_tac ΔphoU strain as a platform to begin characterizing new phoU mutations in plasmids.     

Adaptive Evolution in Producing Microtiter Cultivations Generates Genetically Stable Escherichia coli Production Hosts for Continuous Bioprocessing

The production of recombinant proteins usually reduces cell fitness and the growth rate of producing cells. The growth disadvantage favors faster-growing non-producer mutants. Therefore, continuous bioprocessing is hardly feasible in Escherichia coli due to the high escape rate. The stability of E. coli expression systems under long-term production conditions and how metabolic load triggered by recombinant gene expression influences the characteristics of mutations are investigated. Iterated fed-batch-like microbioreactor cultivations are conducted under production conditions. The easy-to-produce green fluorescent protein (GFP) and a challenging antigen-binding fragment (Fab) are used as model proteins, and BL21(DE3) and BL21^Q strains as expression hosts. In comparative whole-genome sequencing analyses, mutations that allowed cells to grow unhindered despite recombinant protein production are identified. A T7 RNA polymerase expression system is only conditionally suitable for long-term cultivation under production conditions. Mutations leading to non-producers occur in either the T7 RNA polymerase gene or the T7 promoter. The host RNA polymerase-based BL21^Q expression system remains stable in the production of GFP in long-term cultivations. For the production of Fab, mutations in lacI of the BL21^Q derivatives have positive effects on long-term stability. The results indicate that adaptive evolution carried out with genome-integrated E. coli expression systems in microtiter cultivations under industrial-relevant production conditions is an efficient strain development tool for production hosts.     

Topology-informed strategies for the overexpression and purification of membrane proteins

Membrane proteins represent a significant fraction of all genomes and play key roles in many aspects of biology, but their structural analysis has been hampered by difficulties in large-scale production and crystallisation. To overcome the first of these hurdles, we present here a systematic approach for expression and affinity-tagging which takes into account transmembrane topology. Using a set of bacterial transporters with known topologies, we tested the efficacy of a panel of conventional and Gateway? recombinational cloning vectors designed for protein expression under the control of the tac promoter, and for the addition of differing N- and C-terminal affinity tags. For transporters in which both termini are cytoplasmic, C-terminal oligohistidine tagging by recombinational cloning typically yielded functional protein at levels equivalent to or greater than those achieved by conventional cloning. In contrast, it was not effective for examples of the substantial minority of proteins that have one or both termini located on the periplasmic side of the membrane, possibly because of impairment of membrane insertion by the tag and/or att-site-encoded sequences. However, fusion either of an oligohistidine tag to cytoplasmic (but not periplasmic) termini, or of a Strep-tag II peptide to periplasmic termini using conventional cloning vectors did not interfere with membrane insertion, enabling high-level expression of such proteins. In conjunction with use of a C-terminal Lumio? fluorescence tag, which we found to be compatible with both periplasmic and cytoplasmic locations, these findings offer a system for strategic planning of construct design for high throughput expression of membrane proteins for structural genomics projects.     

Metabolic engineering of Escherichia coli for the production of cadaverine: A five carbon diamine

A five carbon linear chain diamine, cadaverine (1,5‐diaminopentane), is an important platform chemical having many applications in chemical industry. Bio‐based production of cadaverine from renewable feedstock is a promising and sustainable alternative to the petroleum‐based chemical synthesis. Here, we report development of a metabolically engineered strain of Escherichia coli that overproduces cadaverine in glucose mineral salts medium. First, cadaverine degradation and utilization pathways were inactivated. Next, L ‐lysine decarboxylase, which converts L ‐lysine directly to cadaverine, was amplified by plasmid‐based overexpression of the cadA gene under the strong tac promoter. Furthermore, the L ‐lysine biosynthetic pool was increased by the overexpression of the dapA gene encoding dihydrodipicolinate synthase through the replacement of the native promoter with the strong trc promoter in the genome. The final engineered strain was able to produce 9.61 g L⁻¹ of cadaverine with a productivity of 0.32 g L⁻¹ h⁻¹ by fed‐batch cultivation. The strategy reported here should be useful for the bio‐based production of cadaverine from renewable resources. Biotechnol. Bioeng. 2011; 108:93–103. © 2010 Wiley Periodicals, Inc.