Expression and purification of truncated, non-glycosylated turkey beta-adrenergic receptors for crystallization

In order to purify milligram quantities of turkey β-adrenergic receptor (βAR) for structural analysis, we have expressed mutant βARs using the baculovirus system. The initial βAR construct was truncated at both N- and C-termini thus removing an N-glycosylation site. Cys 116 was mutated to leucine and a histidine tag was added at the C-terminus resulting in the βAR construct 20-424/His6. Expression of this construct in Sf9 cells produced 0.5 mg of unpurified receptor per liter of culture which necessitated the use of a fermenter for large-scale production. The yield was improved more than 2-fold to 1.2 mg/l culture by using Tni cells which facilitated the production of receptor on a 4 litre scale in shake cultures. The receptor was purified to homogeneity with 35% recovery giving a yield of 2 mg receptor. A further deletion at the N-terminus (βAR 34-424/His6) eliminated proteolysis which had been observed with the original construct and also increased expression more than 5-fold to 360 pmol/mg solubilized membrane protein. This expression level is one of the highest reported for a G protein-coupled receptor (GPCR) and has enabled us to purify 10 mg βAR for large-scale crystallization experiments.     

High-level secretion of dipetarudin, a chimeric thrombin inhibitor, by Pichia pastoris

Dipetarudin is a potent direct thrombin inhibitor that was genetically engineered as a chimera between dipetalogastin II and hirudin. Dipetarudin was initially cloned and purified from Escherichia coli, but with a very low yield of about 0.3 mg/l of culture medium. In this study, we report the production of dipetarudin in the methylotrophic yeast Pichia pastoris using pPIC9 vector. The His+ transformants were screened for the best expression performances by prolongation of the ecarin clotting time. An optimal dipetarudin's expression was reached by addition of methanol in culture medium to a final concentration of 0.5%, every 8h during 4 days. Secreted dipetarudin was purified essentially using a two-step purification scheme: anion exchange chromatography in a Resource Q column, followed by C18-reversed phase HPLC. About 150 mg purified dipetarudin was obtained from 1l culture supernatant. This yield is 500-fold higher than the yield obtained with the E. coli system. The molecular mass of dipetarudin calculated by MALDI-TOF (7450 Da) was in agreement with the mass calculated by the amino acid composition (7454 Da), indicating correct processing of the signal sequence. The Ki value of dipetarudin was 399+/-83 fM, which is in agreement with that calculated for the inhibitor isolated from E. coli. This efficient and cost-effective expression system facilitates large-scale production and purification of dipetarudin for further structural, functional and pharmacological investigations.     

Transfected insect cells in suspension culture rapidly yield moderate quantities of recombinant proteins in protein-free culture medium

Methodology to rapidly express milligram quantities of recombinant proteins through the Lipofectin-mediated transfection of insect cells in small-scale, protein-free suspension culture is presented. The transfection phase in suspension culture was first optimized using the green fluorescence protein coupled with FACs analysis to examine the effect of variables such as the transfection media, duration, and cell density on transfection efficiency and expression level. The recombinant protein production phase was optimized using secreted alkaline phosphatase (SEAP) as a reporter protein to evaluate the cell seeding density and harvest time. Using this method, 5 secreted, 2 intracellular, and 1 chimeric protein were expressed at levels ranging from 6 to 50 mg/L. Furthermore, the ability to purify over 2 mg of His(6)-tagged SEAP by immobilized metal affinity chromatography from 50 mL insect cell culture medium to greater than 95% purity was also demonstrated. This method is suitable for scale-up and high-throughput applications.     

Production of chemokines CTAPIII and NAP/2 by digestion of recombinant ubiquitin-CTAPIII with yeast ubiquitin C-terminal hydrolase and human immunodeficiency virus protease.

Recombinant yeast ubiquitin C-terminal hydrolase (YUH1), which has an N-terminal (His)(6) tag, and an autolysis-resistant mutant of the human immunodeficiency virus-1 protease (HIV-1 Pr) have been used as specific proteases to yield peptides from a ubiquitin conjugate. In the present example, connective tissue-activating peptide (CTAPIII) and neutrophil-activating peptide 2 (NAP/2) were generated by digestion of a ubiquitin-CTAPIII conjugate with YUH1 and HIV Pr, respectively, as indicated below: [see text] YUH1 cleaved at the peptide bond formed by the C-terminal Gly(76) of ubiquitin (Ub) and the N-terminal Asn(1) of the 85-residue peptide CTAPIII. The HIV-1 Pr cleaved between Tyr(15) and Ala(16), the N-terminal Ala of the 70-residue peptide NAP/2. Both enzymes produced authentic peptides from the Ub fusion protein, with a nearly 100% yield. The liberated CTAPIII and NAP/2 were separated from (His)(6)-Ub, the trace amounts of unreacted (His)(6)-Ub-CTAPIII, HIV-1 Pr, and the (His)(6)-YUH1 by passage over a nickel-chelate column; the final yield was about 10 mg of peptide/liter of cell culture. (His)(6)-YUH1, the HIV Pr mutant, and the (His)(6)-Ub-CTAPIII substrate were all expressed individually in Escherichia coli. (His)(6)-YUH1 and (His)(6)-Ub-CTAPIII were highly expressed in a soluble form, but about 75% of the total (His)(6)-YUH1 was also found in inclusion bodies. Both proteins from the soluble fractions were easily purified in a single step by immobilized metal ion affinity chromatography with a yield of about 27 mg of (His)(6)-Ub-CTAPIII and 13.6 mg of (His)(6)-YUH1 protein/liter of cell culture. Chemotactic factor activity, as assessed by the neutrophil shape change assay, was observed for NAP/2, but not for CTAPIII. This strategy, which employs YUH1 and the HIV-1 Pr as tools for the highly selective cleavage of the chimeric substrate, should be applicable to the large-scale production of a variety of peptides.     

Optimized Heterologous Expression of the Polymorphic Human Glutathione Transferase M1-1 Based on Silent Mutations in the Corresponding cDNA

An expression clone for large-scale production of the polymorphic human glutathione transferase (GST) M1-1 has been developed. Heterologous expression inEscherichia coliafforded a yield of 100 mg of GST M1-1 per 3 liters of culture medium, corresponding to an approximately 10-fold increased yield compared to the parental expression construct. Overproduction of the enzyme was dependent on the codon usage in the 5′ region of the DNA sequence encoding glutathione transferase M1-1. High-level expression clones were generated by a combination of random silent mutations in selected wobble positions in the coding sequence and immunoselection of clones from the library of random mutants. The strategy used is generally applicable for the production of recombinant proteins provided that a suitable selection procedure is available for identifying the desired mutants.     

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.     

In vitro expression and site-specific mutagenesis of the cloned human lipoprotein lipase gene. Potential N-linked glycosylation site asparagine 43 is important for both enzyme activity and secretion

Detailed structure-function information about human lipoprotein lipase (LPL) is unavailable because it is difficult to purify large amounts of the enzyme for study. To circumvent this problem, we constructed an in vitro LPL expression vector. Human LPL cDNA was cloned and inserted into the expression vector p91023(B). After transfection of COS M-6 cells with the human LPL cDNA construct, LPL enzyme activity was detected in cell extracts and culture medium. Purified human apolipoprotein C-II caused a 5-fold stimulation of the recombinant human LPL expressed in vitro. Using site-specific mutagenesis, Ala residues were substituted for Asn residues at two potential N-linked glycosylation sites (positions 43 and 359) and at a third unrelated Asn (position 257) in the LPL cDNA. RNA blot analysis demonstrated the presence of a single mRNA species in COS cells transfected with wild-type and mutant LPL expression vectors. Intracellular and secreted LPL activity was absent in the construct containing an Ala for Asn mutation at position 43, whereas the same substitutions at positions 257 and 359 did not appreciably affect activity. LPL activity was also absent in another construct containing a Gln for Asn mutation at position 43. Quantitation of LPL protein mass concomitant with measurement of enzyme activity showed that substitution of Ala or Gln for Asn at position 43 resulted in the production of an enzymatically inactive protein which accumulated intracellularly but was not secreted into the culture medium. Our report represents an initial documentation of the expression of cloned human LPL in vitro and of the importance of Asn-43 for both enzyme activity and secretion.     

Improved yields for baculovirus-mediated expression of human His(6)-PDK1 and His(6)-PKBbeta/Akt2 and characterization of phospho-specific isoforms for design of inhibitors that stabilize inactive conformations

PDK1 and PKB/Akt have a pleckstrin homology (PH) domain at the C-terminus and N-terminus, respectively, which stabilizes an unphosphorylated, autoinhibited conformation. Binding of the PH domain to a phospholipid second messenger causes relief of autoinhibition, which results in kinase phosphorylation and activation. Baculovirus-mediated expression in Sf9 insect cells of both His(6)-PDK1 and His(6)-PKBbeta/Akt2 were optimized, which significantly improved the yields (5-fold) of the affinity purified enzymes over previously reported values. Isoelectric focusing (IEF) and Western analyses indicated that the apparent V(max)=192+/-13 U/mg and K(m) (PDK-Tide)=55+/-10 microM of purified His(6)-PDK1 results from a mixture of at least three different phospho-specific isoforms (pI values of 6.8, 6.5, and 6.4). A purely unphosphorylated isoform of His(6)-PDK1 (pI=6.8) was generated by treatment with lambda protein phosphatase (lambdaPP), which decreased V(max) to 2.4+/-0.4 U/mg and increased K(m) (PDK-Tide) to 217+/-61 microM. Isoelectric focusing and Western analyses indicated that the apparent V(max)=0.21+/-0.03 U/mg and K(m) (Crosstide)=87+/-30 microM of purified His(6)-PKBbeta/Akt2 results from a mixture of the enzyme monophosphorylated either at Ser-474 ( approximately 90%) or at Thr-309 ( approximately 10%). A purely unphosphorylated isoform of His(6)-PKBbeta/Akt2 (pI=6.4) was generated by treatment with lambdaPP, which decreased V(max) approximately 2-fold. The optimization of high-level production and detailed characterization of purified and lambdaPP-treated His(6)-PDK1 and His(6)-PKBbeta/Akt2 will facilitate detailed structural and kinetic studies aimed at understanding the mechanism of second messenger-induced activation.     

Multi-Host Expression System for Recombinant Production of Challenging Proteins

Recombinant production of complex eukaryotic proteins for structural analyses typically requires a profound screening process to identify suitable constructs for the expression of ample amounts of properly folded protein. Furthermore, the evaluation of an optimal expression host has a major impact on protein yield and quality as well as on actual cost of the production process. Here we present a novel fast expression system for multiple hosts based on a single donor vector termed pFlp-Bac-to-Mam. The range of applications of pFlp-Bac-to-Mam comprises highly efficient transient transfection of HEK293-6E in serum-free suspension culture and subsequent large-scale production of challenging proteins expressing in mg per Liter level using either the baculoviral expression vector system or stable CHO production cell lines generated by Flp-mediated cassette exchange. The success of the multi-host expression vector to identify the optimal expression strategy for efficient production of high quality protein is demonstrated in a comparative expression study of three model proteins representing different protein classes: intracellular expression using a fluorescent protein, secretion of a single-chain-Fv-hIgG1Fc fusion construct and production of a large amount of highly homogeneous protein sample of the extracellular domain of a Toll-like receptor. The evaluation of the production efficiency shows that the pFlp-Bac-to-Mam system allows a fast and individual optimization of the expression strategy for each protein class.     

Receptor number and caveolar co-localization determine receptor coupling efficiency to adenylyl cyclase

Recent evidence suggests that many signaling molecules localize in microdomains of the plasma membrane, particularly caveolae. In this study, overexpression of adenylyl cyclase was used as a functional probe of G protein-coupled receptor (GPCR) compartmentation. We found that three endogenous receptors in neonatal rat cardiomyocytes couple with different levels of efficiency to the activation of adenylyl cyclase type 6 (AC6), which localizes to caveolin-rich membrane fractions. Overexpression of AC6 enhanced the maximal cAMP response to beta(1)-adrenergic receptor (beta(1)AR)-selective activation 3.7-fold, to beta(2)AR-selective activation only 1.6-fold and to prostaglandin E(2) (PGE(2)) not at all. Therefore, the rank order of efficacy in coupling to AC6 is beta(1)AR > beta(2)AR > prostaglandin E(2) receptor (EP(2)R). beta(2)AR coupling efficiency was greater when we overexpressed the receptor or blocked its desensitization by expressing betaARKct, an inhibitor of G protein-coupled receptor kinase activation, but was not significantly greater when cells were treated with pertussis toxin. Assessment of receptor and AC expression indicated co-localization of AC5/6, beta(1)AR, and beta(2)AR, but not EP(2)R, in caveolin-rich membranes and caveolin-3 immunoprecipitates, likely explaining the observed activation of AC6 by betaAR subtypes but lack thereof by PGE(2). When cardiomyocytes were stimulated with a betaAR agonist, beta(2)AR were no longer found in caveolin-3 immunoprecipitates; an effect that was blocked by expression of betaARKct. Thus, agonist-induced translocation of beta(2)AR out of caveolae causes a sequestration of receptor from effector and likely contributes to the lower efficacy of beta(2)AR coupling to AC6 as compared with beta(1)AR, which do not similarly translocate. Therefore, spatial co-localization is a key determinant of efficiency of coupling by particular extracellular signals to activation of GPCR-linked effectors.     

Cloning, Large Scale Over-Expression in E. coli and Purification of the Components of the Human LAT 1 (SLC7A5) Amino Acid Transporter

The high yield expression of the human LAT1 transporter has been obtained for the first time using E. coli. The hLAT1 cDNA was amplified from HEK293 cells and cloned in pH6EX3 vector. The construct pH6EX3-6His-hLAT1 was used to express the 6His-hLAT1 protein in the Rosetta(DE3)pLysS strain of E. coli. The highest level of expression was detected 8 h after induction by IPTG at 28 °C. The expressed protein was collected in the insoluble fraction of cell lysate. On SDS-PAGE the apparent molecular mass of the polypeptide was 40 kDa. After solubilization with sarkosyl and denaturation with urea the protein carrying a 6His N-terminal tag was purified by Ni²⁺-chelating affinity chromatography and identified by anti-His antibody. The yield of the over-expressed protein after purification was 3.5 mg/L (cell culture). The human CD98 cDNA amplified from Imagene plasmid was cloned in pGEX-4T1. The construct pGEX-4T1-hCD98 was used to express the GST-hCD98 protein in the Rosetta(DE3)pLysS strain of E. coli. The highest level of expression was detected in this case 4 h after induction by IPTG at 28 °C. The expressed protein was accumulated in the soluble fraction of cell lysate. The molecular mass was determined on the basis of marker proteins on SDS-PAGE; it was about 110 kDa. GST was cleaved from the protein construct by incubation with thrombin for 12 h and the hCD98 was separated by Sephadex G-200 chromatography (size exclusion). hCD98 showed a 62 kDa apparent molecular mass, as determined on the basis of molecular mass markers using SDS-PAGE. The yield of CD98 was 2 mg/L of cell culture.     

Expression, purification, characterization and crystallization of a recombinant human cytosolic beta-glucosidase produced in insect cells

Human cytosolic beta-glucosidase is a monomeric enzyme that hydrolyzes various beta-d-glycosides and its real physiological role remains unclear. Here, we describe the production of this enzyme in Sf9 cells with a N-terminal 6x His tag. The production yield of the recombinant protein was in the 10 to 30 mg/l range. The protein was purified to homogeneity using two chromatographic steps, taking advantage of the 6x His tag in the first step, then using the physical and chemical properties of the protein for ionic exchange. Gel filtration analysis revealed that the protein is monomeric as expected. The kinetic parameters for 4-methylumbelliferyl beta-L-glucopyranoside, VM and KM, were measured (KM=32 microM and VM=157 micromol/h/mg at pH 7.0) and found similar to those reported for either the natural isolated enzyme or the recombinant protein expressed in COS7 cells (KM of 60-70 microM and 40 microM, respectively). Protein crystals were obtained and are now under structural investigations. In summary, we set up a heterologous expression system in Sf9 insect cells allowing the expression and production of large amounts of a pure active human protein, suitable for crystallographic studies.     

Inducing single-cell suspension of BTI-TN5B1-4 insect cells: I. The use of sulfated polyanions to prevent cell aggregation and enhance recombinant protein production

Sulfated polyanions have been successfully used to rapidly obtain and maintain stable single-cell suspension of BTI-TN5B1-4 cells, a cell line which has a high intrinsic capacity for recombinant protein production but clumps severely in suspension reducing its effectiveness as a host for foreign protein production with the baculovirus expression vector system. The efficacy of inducing single-cell suspension correlated positively with the increase in sulfation of the added polyanion. Unsulfated polyanions, neutral polymers, polycations, disaccharides, and monosaccharides were ineffective in inducing single-cell suspension.Elimination of clumping in suspension culture by adding a dispersing agent can lead to enhanced recombinant protein production. Inducing single-cell suspension with dextran sulfate, a highly sulfated polyanion, resulted in a four-fold increase in volumetric yield of the recombinant glycosylated protein, human secreted alkaline phosphatase, and a two-fold increase in volumetric yield of the recombinant cytoplasmic protein, beta-galactosidase. High yields of 82 U/ml (ca. 110 mg/L) for alkaline phosphatase, and 705 U/mL (ca. 2.3 g/L) for beta-galactosidase under elevated oxygen have been obtained. The optimum volumetric yield of alkaline phosphatase in BTI-TN5B1-4 dextran sulfate cells under elevated oxygen but unsupplemented medium is 6 to 11-fold higher than attached cultures, and 3-fold higher than the best yield obtained for SF21 cells in suspension at elevated oxygen and with nutrient supplementation. More importantly, cells can be infected at high density without complications from aggregation, which has important implications for scale-up. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54:191-205, 1997.     

Large-scale preparation of recombinant platelet-derived growth factor AA secreted from recombinant baby hamster kidney cells

The short isoform of platelet-derived growth factor A (PDGF-A) was expressed in a mammalian host (BHK-21 cell). A cell line was obtained that secreted up to 0.3 micrograms/10(6) cells recombinant PDGF-A chain homodimer/day into the medium. For large-scale production of supernatant, cells were grown either in roller bottles or in 2.5-1 stirred tank fermenters. A simple two-step procedure was developed to purify recombinant PDGF-AA (rPDGF-AA). The first step was adsorption onto porous glass and the final step was reversed-phase high-performance liquid chromatography. The yield was 0.2 mg/l supernatant. A total amount of 20-30 mg pure rPDGF-AA may be obtained from a single fermenter run. Sequence analysis showed the correct amino terminus and no internal proteolytic cleavages. The specific activity was 5 ng/ml for mouse AKR-2B cells. [125I]rPDGF-AA had an affinity constant of approximately 0.5 nM to these cells and 25,000 binding sites were estimated/cell.     

Improved yields of full-length functional human FGF1 can be achieved using the methylotrophic yeast Pichia pastoris

We have produced human fibroblast growth factor 1 (hFGF1) in the methylotrophic yeast Pichia pastoris in order to obtain the large amounts of active protein required for subsequent functional and structural characterization. Four constructs were made to examine both intracellular and secreted expression, with variations in the location of the His6 tag at either end of the peptide. hFGF1 could be produced from all four constructs in shake flasks, but production was optimized by growing only the highest-yielding of these strains, which produced hFGF1 intracellularly, under tightly controlled conditions in a 3 L fermentor. One hundred and eight milligrams of pure protein was achieved per liter culture (corresponding to 0.68 mg of protein per gram of wet cells), the function of which was verified using NIH 3T3 cell cultures. This is a 30-fold improvement over previously reported yields of full-length hFGF1.     

Enhancement of taxol production and release in Taxus chinensis cell cultures by ultrasound,methyl jasmonate and in situ solvent extraction

This study evaluates the use of a novel mechanical stimulus, ultrasound (US), and a putative chemical elicitor, methyl jasmonate (MJ), combined with in situ solvent extraction (two-phase culture), to enhance taxol production by Taxus chinensis cells in suspension culture. The volumetric taxol yield was increased 1.5- to 1.8-fold with 2 min US treatment once or twice during a 4-week culture period, about 5-fold with 60-120 microM MJ, and 7- to 9-fold by in situ solvent extraction of taxol with dibutyl phthalate (DBP) (11% v/v). The percent of extracellular taxol or taxol release was also significantly increased. The combined use of US (day 5 or 9) and MJ treatment (day 7) resulted in taxol yields 20-50% higher than each of the treatments used alone. The most favorable strategy for taxol production was the application of US or MJ treatment, followed by in situ solvent extraction, giving rise to a taxol yield of 33-35 mg/l, about 17-fold higher than the control, at 1.9 mg/l. It was found that the organic solvent DBP, as well as US and MJ, stimulated the enzyme activity of secondary metabolic pathways, which was partially responsible for the enhanced taxol production.     

Single step purification of a wheat 9 kDa lipid transfer protein secreted by Pichia pastoris

Pichia pastoris produced large quantities of a wheat 9 kDa lipid transfer protein as a recombinant secreted protein. A single step procedure applying the yeast culture directly to expanded-bed Streamline SP-XL was used to purify it 4 times. From 700 ml of culture, 476 mg of highly purified LTP were obtained in one day. This represents a 6-fold higher yield in comparison to the five days purification scheme it replaces.     

Stimulation of monoclonal antibody production by human-human hybridoma cells with an elevated concentration of potassium or sodium phosphate in serum-free medium

Potassium or sodium phosphate was found to stimulate the production of human monoclonal antibody by human-human hybridoma HB4C5. The addition of 15 mM Na-phosphate (pH 7.4) into serum-free culture medium increased the antibody production up to 4-fold, when seeded at cell density of 1×10⁵ cells/ml in dishes. At the higher cell density of 5×10⁵ cells/ml, K-phosphate was more effective than Na-phosphate, at the same concentration. In large-scale continuous culture, the addition of 10 mM Na-phosphate into serum-free culture medium stimulated antibody production by HB4C5 cells 6-fold.