Studies on the production of lipase from recombinant Staphylococcus carnosus

Summary Production of lipase from recombinant Staphylococcus carnosus pLipPS2 was studied in standard stirred tank bioreactors. Only low lipase activity was obtained under conventional operating conditions, i.e., moderate to high stirring speeds and aeration rates for keeping the dissolved oxygen concentration at high levels. Additional targetted experiments indicated that the reason for the observed low lipase activity is lipase inactivation due to surface forces and shear stress at the gas/liquid interface. Therefore, a cultivation strategy is proposed that minimizes gas/liquid interfacial area and maximizes the driving concentration for O₂ mass transfer by controlling the dissolved oxygen to low values by gentle stirring and low aeration rates. Thus, high lipase activities can be obtained even in larger scale standard stirred tank bioreactors. Offprint requests to: W.-D. Deckwer     

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.     

Cell surface display of recombinant proteins on Staphylococcus carnosus.

A novel expression system for surface display of heterologous proteins on Staphylococcus carnosus cells has been developed. Taking advantage of the promoter and secretion signals, including a propeptide region, from the lipase gene of Staphylococcus hyicus and the cell wall-spanning and membrane-binding region of protein A from Staphylococcus aureus, efficient surface display of an 80-amino-acid peptide from a malaria blood stage antigen could be achieved. A serum albumin binding protein from streptococcal protein G was used both as a general reporter molecule and to increase the accessibility of the surface-displayed proteins. Immunoblotting, immunogold staining, and immunofluorescence on intact recombinant S. carnosus cells verified the presence of the propeptide, the malaria antigen, and the albumin-binding reporter protein on the bacterial surface. For the first time, fluorescence-activated cell sorting was used to analyze the presence of surface-displayed hybrid receptors on gram-positive bacteria.     

Lipase production of Staphylococcus carnosus in a dialysis fermentor

Summary In a newly constructed one-vessel dialysis fermentor, a strain of Staphylococcus carnosus TM300 carrying the lipase secretion plasmid pLipPS1 was used to investigate exoenzyme and biomass production. The bacterial culture grows in an inner compartment of 21 volume, separated from a 101 nutrient broth compartment by a conventional dialysis membrane. In order to avoid substrate depletion and to prolong the growth phase, a highly concentrated nutrient broth was used. The biomass production reached 60 g cell dry weight/l. The increase in extracellular lipase concentration was directly coupled with the increase of cell mass and reached a value of 230 mg/l culture supernatant. Harvesting the cells in the late growth phase, the lipase content was about 30% of the total exoproteins in the supernatant.     

Self-cleaving fusion tags for recombinant protein production

Fusion expression is a common practice for recombinant protein production. Some fusion tags confer solubility on the target protein whereas others provide affinity handles that facilitate purification. However, the tag usually needs to be removed from the final product, which involves using expensive proteases or hazardous chemicals and requires additional chromatography steps. Self-cleaving tags are a special group of fusion tags that possess inducible proteolytic activity. Combined with appropriate affinity tags, they enable fusion purification, cleavage and target separation to be achieved in a single step, which saves time, labor and cost. This paper reviews currently available self-cleaving fusion tags for recombinant protein production. For each system, an introduction of its key characteristics and a brief discussion of its advantages and disadvantages is given.     

A fusion protein system for the recombinant production of short disulfide-containing peptides

A recombinant fusion protein system for the production, oxidation, and purification of short peptides containing a single disulfide bond is described. The peptides are initially expressed in Escherichia coli as a fusion to an engineered mutant of the N-terminal SH2 domain of the intracellular phosphatase, SHP-2. This small protein domain confers several important properties which facilitate the production of disulfide-containing peptides: (i) it is expressed at high levels in E. coli; (ii) it can be purified via a hexahistidine tag and reverse-phase HPLC; (iii) it contains no endogenous cysteine residues, allowing the formation of an intrapeptide disulfide bond while still attached to the fusion partner; (iv) it is highly soluble in native buffers, facilitating the production of very hydrophobic peptides and the direct use of fusion products in biochemical assays; (v) it contains a unique methionine residue at the junction of the peptide and fusion partner to facilitate peptide cleavage by treatment with cyanogen bromide (CNBr). This method is useful for producing peptides, which are otherwise difficult to prepare through traditional chemical synthesis approaches, and this has been demonstrated by preparing a number of hydrophobic disulfide-containing peptides derived from phage-display libraries.     

High expression of a recombinant human calcitonin precursor peptide in Escherichia coli

Human calcitonin (hCT) is a C-terminus -amidated peptide hormone consisting of 32 amino acids. The amidated structure is essential for its biological activities, and the C-terminal-glycine-extended precursor peptide, hCT[G], is converted to bioactive hCT by a C-terminus--amidating enzyme. An efficient production method is described for the hCT[G] peptide, as a part of the fusion protein consisting of a modified E. coli -galactosidase, linker amino acids and hCT[G]. Stable inclusion bodies of the fusion protein in E. coli were expressed by focusing on the amino acid charge, and the fusion protein was modified by inserting a basic amino acid sequence into its linker region. This modification greatly affected the formation of inclusion bodies. E. coli strain W3110/pG97S4DhCT [G]R4 could produce a large amount of stable inclusion bodies, and the hCT[G] peptide was released quantitatively from the fusion protein by S. aureus V8 protease. This enabled a large-scale production method to be established for the hCT[G] precursor peptide in E. coli to produce mature hCT.     

A fusion protein system for the recombinant production of short disulfide bond rich cystine knot peptides using barnase as a purification handle

The inhibitor cystine knot (ICK) structural motif has been found in several small proteins and peptides from plants, insects, marine molluscs, and also in human. It is defined by a triple beta-sheet that is held together by three intramolecular disulfide bonds built by six conserved cysteine residues that generate a highly rigid and stable fold. We describe a procedure for the production of ICK peptides with correct disulfide bond connectivities via expression in Escherichia coli as fusion proteins with an enzymatically inactive variant of the Bacillus amyloliquefaciens RNAse barnase. Barnase directs the fused peptide to the culture medium and the fusion protein can be isolated by combined cation exchange/reverse-phase chromatography. The ICK peptides are released from the barnase expression and purification handle either by cyanogen bromide or by protease cleavage to give pure and correctly folded cystine knot peptides.     

Maltose-binding protein enhances secretion of recombinant human granzyme B accompanied by in vivo processing of a precursor MBP fusion protein

Background

The apoptosis-inducing serine protease granzyme B (GrB) is an important factor contributing to lysis of target cells by cytotoxic lymphocytes. Expression of enzymatically active GrB in recombinant form is a prerequisite for functional analysis and application of GrB for therapeutic purposes.

Methods and Findings

We investigated the influence of bacterial maltose-binding protein (MBP) fused to GrB via a synthetic furin recognition motif on the expression of the MBP fusion protein also containing an N-terminal α-factor signal peptide in the yeast Pichia pastoris. MBP markedly enhanced the amount of GrB secreted into culture supernatant, which was not the case when GrB was fused to GST. MBP-GrB fusion protein was cleaved during secretion by an endogenous furin-like proteolytic activity in vivo, liberating enzymatically active GrB without the need of subsequent in vitro processing. Similar results were obtained upon expression of a recombinant fragment of the ErbB2/HER2 receptor protein or GST as MBP fusions.

Conclusions

Our results demonstrate that combination of MBP as a solubility enhancer with specific in vivo cleavage augments secretion of processed and functionally active proteins from yeast. This strategy may be generally applicable to improve folding and increase yields of recombinant proteins.     

Characterization of the molybdate transport system ModABC of Staphylococcus carnosus

Transposon mutagenesis of Staphylococcus carnosus led to the identification of three genes, modABC, which encode an ABC transporter that is involved in molybdate transport. It was shown by [¹⁴C]palmitate labeling that ModA represents a lipoprotein that in gram-positive bacteria is the counterpart of the periplasmic binding proteins of gram-negative organisms. The sequence characteristics identify ModB as the integral-membrane, channel-forming protein and ModC as the ATP-binding energizer for the transport system. Mutants defective in modABC had only 0.4% of the wild-type nitrate reductase activity. Molybdate at a non-physiologically high concentration (100 μM) fully restored nitrate reductase activity, suggesting that at least one other system is able to transport molybdate, but with lower affinity. The expression of modA (and most likely of modBC) was independent of oxygen and nitrate. To date, there are no indications for molybdate-specific regulation of modABC expression since in a modB mutant, modA expression was unchanged in comparison to the wild-type. Received: 5 February 1999 / Accepted: 31 May 1999     

An efficient trypsin digestion strategy for improving desB30 productivity from recombinant human insulin precursor fusion protein

The insulin precursor (IP) expressed in Pichia pastoris is a single-chain peptide fused with a spacer peptide (EEAEAEAEPK) localized at its N-terminus and containing three trypsin cleavage sites in the polypeptide chain. The IP fusion protein is trypsinized to generate the insulin product desB30, which has a deletion of threonine^B30. The three restriction sites on IP fusion protein had different affinities for trypsin and were digested in sequential order. Further analysis showed that approximately 20% of the IP digestion intermediates could not be converted into the final desB30 product if the IP fusion protein was digested in an aqueous phase. This result can be attributed to the formation of IP dimers or hexamers, which could restrict enzyme reactivity in the aqueous phase. To enhance the conversion yield of the IP fusion protein to desB30 products, a new digestion method was established. The IP was digested in the eluent that resulted from reverse phase chromatography during the purification process, which improved the yield of digestion from 80.2% to 95.6%.     

一种新型改良硫氧还蛋白融合表达体系的建立及cathelicidin家族Lf-CATH2的表达

通过改良硫氧还蛋白融合表达体系,原核表达cathelicidin家族抗菌肽Lf-CATH2。首先在Lf-CATH2基因上游加入凝血酶位点,并去除p ET32α载体的凝血酶序列和S标签序列,构建优化的Lf-CATH2-p ET32α-TS载体,于大肠杆菌中表达。产物融合蛋白经凝血酶切割释放Lf-CATH2,纯化后进行抗菌活性检测。结果表明改良的硫氧还蛋白融合表达体系显著提高酶切效率达37%,Lf-CATH2在新体系中获得了可溶性高表达,且保留了抗菌活性。因此该新型硫氧还蛋白融合表达体系,有望为cathelicidin家族及其他阳离子活性肽提供更好的原核表达载体工具。     

Fed-batch production of thermomonospora fusca endoglucanase by recombinant streptomyces lividans

The factors affecting the production of a Thermomonospora fusca endoglucanase by a recombinant Streptomyces lividans strain were studied in a fermentor with glucose addition controlled by a pH-stat. The recombinant plasmid was stable for 35 generations with constant endoglucanase productivity. Glucose and peptone were used as the carbon and nitrogen sources. Addition of Tween-80 increased endoglucanase production twofold. A significant decrease in endoglucanase production was observed at low aeration. During fed-batch cultivation, pulse feeding (6 g/L) of a glucose-ammonium sulfate solution was optimal for endoglucanase production. With higher concentrations of glucose (15 g/L), a significant amount of organic acid, including acetic acid, was produced, which inhibited cell growth and endoglucanase production. Under optimum conditions, 1.7 U/mL of endoglucanase were produced. Copyright 1998 John Wiley & Sons, Inc.     

Enhanced production of recombinant Staphylococcus simulans lysostaphin using medium engineering

Abstract

Staphylococcus aureus, among other staphylococcal species, developed multidrug resistance and causes serious health risks that require complex treatments. Therefore, the development of novel and effective strategies to combat these bacteria has been gaining importance. Since Staphylococcus simulans lysostaphin is a peptidoglycan hydrolase effective against staphylococcal species, the enzyme has a significant potential for biotechnological applications. Despite promising results of lysostaphin as a bacteriocin capable of killing staphylococcal pathogens, it is still not widely used in healthcare settings due to its high production cost. In this study, medium engineering techniques were applied to improve the expression yield of recombinant lysostaphin in E. coli. A new effective inducible araBAD promoter system and different mediums were used to enhance lysostaphin production. Our results showed that the composition of autoinduction media enhanced the amount of lysostaphin production 5-fold with the highest level of active lysostaphin at 30?°C. The production cost of 1000?U of lysostaphin was determined as 4-fold lower than the previously proposed technologies. Therefore, the currently developed bench scale study has a great potential as a large-scale fermentation procedure to produce lysostaphin efficiently.     

Optimization of electroporation-mediated transformation: Staphylococcus carnosus as model organism

AIMS: The study was conducted with an aim to optimize the transformation efficiency of the Gram-positive bacterium Staphylococcus carnosus to a level that would enable the creation of cell surface displayed combinatorial protein libraries. METHODS AND RESULTS: We have thoroughly investigated a number of different parameters for: (i) the preparation of electrocompetent cells; (ii) the treatment of cells before electroporation; (iii) the electroporation step itself; and (iv) improved recovery of transformed cells. Furthermore, a method for heat-induced inactivation of the host cell restriction system was devised to allow efficient transformation of the staphylococci with DNA prepared from other species, such as Escherichia coli. Previously described protocols for S. carnosus, giving transformation frequencies of approximately 10(2) transformants per transformation could be improved to reproducible procedures giving around 10(6) transformants for a single electroporation event, using plasmid DNA prepared from either S. carnosus or E. coli. The transformed staphylococcal cells were analysed using flow cytometry to verify that the entire cell population retained the introduced plasmid DNA and expressed the recombinant protein in a functional form on the cell surface at the same level as the positive control population. CONCLUSIONS: The results demonstrate that the transformation frequency for S. carnosus could be dramatically increased through optimization of the entire electroporation process, and that the restriction barrier for interspecies DNA transfer, could be inactivated by heat treatment of the cells prior to electroporation. SIGNIFICANCE AND IMPACT OF THE STUDY: The generation of large combinatorial protein libraries, displayed on the surface of S. carnosus can be envisioned in the near future, thus dramatically improving the selection compared with the traditional biopanning procedure used in phage display.     

Predictive tool for recombinant protein production in Escherichia coli shake-flask cultures using an on-line monitoring system

As Escherichia coli (E. coli) is well defined with respect to its genome and metabolism, it is a favored host organism for recombinant protein production. However, many processes for recombinant protein production run under suboptimal conditions caused by wrong or incomplete information from an improper screening procedure, because appropriate on-line monitoring systems are still lacking. In this study, the oxygen transfer rate (OTR), determined on-line in shake flasks by applying a respiration activity monitoring system (RAMOS) device, was used to characterize the metabolic state of the recombinant organisms. Sixteen clones of E. coli SCS1 with foreign gene sequences, encoding for different target proteins, were cultivated in an autoinduction medium, containing glucose, lactose, and glycerol, to identify relationships between respiration activity and target protein production. All 16 clones showed a remarkably different respiration activity, biomass, and protein formation under induced conditions. However, the clones could be classified into three distinct types, and correlations could be made between OTR patterns and target protein production. For two of the three types, a decrease of the target protein was observed, after the optimal harvest time had passed. The acquired knowledge was used to modify the autoinduction medium to increase the product yield. Additional 1.5 g/L glucose accelerated the production process for one clone, shifting the time point of the maximal product yield from 24 to 17 h. For another clone, lactose addition led to higher volumetric product yields, in fact 25 and 38% more recombinant protein for 2 and 6 g/L additional lactose, respectively.     

Improvement of recombinant protein production with the human adenovirus/293S expression system using fed-batch strategies

The human adenovirus/293S cell expression system is used for the production of either recombinant protein or adenovirus vectors for use in gene therapy. In this work, the production of protein tyrosine phosphatase (PTP1C) was used as a model for the scale-up of both applications. Maximum specific production of 30 to 45 mug of active protein/10(6) cells was maintained upon infection with adenovirus vectors at cell densities between 2 x 10(6) to 3 x 10(6) cells/mL in a 3.5-L bioreactor. This was achieved by resuspending the culture in fresh medium at infection time. The pH was kept at 7.0 throughout the experiment and, at 24 h postinfection, glucose and essential amino acids were added. Attempts to replace the complete change of medium at the time of infection with nutrient supplementation of the used medium led to lower production levels, suggesting that protein expression was limited not by the absence of a key nutrient but by inhibitory factors. Two potentially inhibitory factors were investigated: lactic acid accumulation and increased osmolarity. Medium acidification such as that which would be brought about by lactic acid accumulation was shown to depress PTP1C production. The lactate molecule itself decreased the cell viability when added in concentrations of 20 mM or more. But the specific productivity was affected at higher lactate concentrations of 40 mM or more. Additions of glucose, amino acids, and NaHCO(3) used to control pH, led to increases in osmolarity. Osmolarities above 400 mOsm lowered cell density. However, specific production was not significantly affected below 500 mOsm. But, at 500 mOsm, PTP1C production peak was shifted from 48 to 72 hpi. Because of the cell loss, this per cell yield increase did not translate into higher volumetric production. When glucose concentrations was kept at 5 mM by fed-batch addition, lactate production and increases in osmolarity were reduced. In shake flasks, this method permitted maximum production with cells resuspended either in fresh or spent medium at infection. This fed-batch process was implemented successfully at the 3.5-L scale. Fed-batch with glucose may provide a means to increase infected-cell density beyond 3 x 10(6) cells/mL.