Nitrogen catabolite repressible GAP1 promoter, a new tool for efficient recombinant protein production in S. cerevisiae
© Debailleul et al.; licensee BioMed Central Ltd. 2013
Received: 30 May 2013
Accepted: 18 December 2013
Published: 26 December 2013
Decades of work requiring heterologous expression of eukaryotic proteins have shown that no expression system can be considered as the panacea and the appropriate expression strategy is often protein-dependent. In a large number of cases, yeasts have proven to be reliable organisms for heterologous protein expression by combining eukaryotic cellular organization with the ease of use of simpler microorganisms.
During this work, a novel promoter system based on the nitrogen catabolite regulation has been developed to produce the general amino acid permease (Gap1) in its natural host, the yeast Saccharomyces cerevisiae. A simple purification protocol was also established that allows to purify milligrams of Gap1 from cells cultivated in a five liters bio-reactor. In order to test the ability of the system to be used for expression of other proteins, the yeast specific transporter of γ-aminobutyric acid (Uga4), a human vesicular transporter of glutamate (Vglut1) and a small secreted glycoprotein (MD-2) were also expressed using the nitrogen catabolite regulation. All proteins were fused to GFP and their presence and localization were confirmed by western blot analysis and fluorescence microscopy.
Our work shows that the nitrogen catabolite repressible GAP1 promoter can be used to obtain high levels of recombinant protein while allowing for large biomass production in S. cerevisiae. This approach can be used to express membrane and soluble proteins from higher eukaryotes (from yeast to human). Therefore, this system stands as a promising alternative to commonly used expression procedure in yeasts.
KeywordsSaccharomyces cerevisiae Protein expression Protein purification Heterologous expression
Genes coding for membrane proteins account for 20% to 30% of all Open Reading Frames present in sequenced genomes  and membrane proteins represent more than 60% of the drug targets but about only 1% of known protein structures [2, 3]. Expression, purification and crystallization of these proteins remain a difficult task to achieve and are very protein-dependent. Importantly, membrane proteins of known structure are mostly of prokaryotic origin, probably due to the difficulties associated with the expression of eukaryotic proteins in scalable systems. Yeasts, and Saccharomyces cerevisiae in particular, have notably proven to be a reliable system of expression for both endogenous and heterologous eukaryotic proteins [4–7]. The extensive knowledge in S. cerevisiae regulation and synthetic pathways, combined with the reduced cost associated with this type of organism, allows to tailor adaptive protocols for the expression of proteins [8, 9].
As any other eukaryotic organism, yeasts possess a typical internal organization with membrane-delimited organelles. Membrane proteins destined to the plasma membrane traffic through the endoplasmic reticulum and Golgi apparatus and eventually undergo post-translational modifications similar to those occurring in higher eukaryotes, although proteins tend to be over-glycosylated when expressed in yeasts [10, 11]. As unicellular and simple organisms, yeasts are very easy to grow and cultures are cost-effective. S. cerevisiae in particular has been used and studied for many years and a wide range of mutants and deletion strains are available. Moreover, a large number of expression vectors are available for protein production in S. cerevisiae and transformation-associated in vivo recombination in these vectors allows to easily test various plasmid constructs (harboring alternative gene promoters, tags, linkers, and eventually including mutations in the genes of interest). Although the biomass obtained from expressing cells can be lower than for other yeasts (such as Pichia pastoris), the relative amount of protein of interest versus the total biomass can result in better purification yield and purity .
Here we developed a novel promoter system in S. cerevisiae aiming at producing large quantities of recombinant membrane or soluble proteins. We originally designed the system for Gap1, the general amino acid permease of S. cerevisiae[13, 14]. Gap1 is a member of the amino acid-polyamine-organocation (APC) superfamily. It can mediate uptake of all protein amino acids, several non-protein amino acids (e.g., ornithine, citrulline, gamma-aminobutyic acid, beta-alanine) and toxic analogs. Gap1 shows very high affinity for most of its natural substrates, with apparent Km values in the micromolar range . These properties are well suited to the physiological role of Gap1, which is synthesized and most active under conditions of poor nitrogen supply (e.g. proline, urea, low ammonium, etc.). The role of Gap1 under these conditions is to scavenge external amino acids in order to be used as nitrogen sources or directly as building blocks for protein synthesis. Transcription of the GAP1 gene is promoted by two GATA-family factors, Gln3 and Gat1, which are mostly active when the nitrogen supply conditions are cell-growth limiting. If cells shift to more favorable nitrogen supply conditions, the Gln3 and Gat1 factors are inhibited by the mechanisms of Nitrogen Catabolite Repression (NCR), leading to a strong decrease in GAP1’s expression .
This conditional transcription was used to design an inducible promoter system in S. cerevisiae where first, biomass is accumulated while expression of the target protein is strongly repressed and, secondly, expression is triggered following an appropriate medium change. Practically, cells were cultivated in a bio-reactor on a rich medium (based on yeast extract and Bactopeptone) containing large quantities of amino acids and other biosynthetic precursors (thus providing optimal nitrogen supply conditions) and glucose as carbon source. Under these conditions, yeasts follow a two-phase growth : they first metabolize glucose by fermentation (even in the presence of oxygen) and then switch to a fully respiratory metabolism. This switch, also referred to as diauxic switch, can be detected by measuring the oxygen concentration in the medium. After biomass accumulation until the diauxic switch, expression of the target protein is triggered by exchanging the rich medium for a defined medium containing a secondary (poor) source of nitrogen.
Based on our expression results with Gap1, we subsequently extended this expression system to three unrelated proteins: the yeast specific transporter of γ-aminobutyric acid (GABA) (Uga4, ), a human vesicular transporter of glutamate (Vglut1, [18, 19]) and a small human secreted glycoprotein (MD-2, [20, 21]). These proteins were expressed under the regulation of the Gap1 promoter and their expression was tested by immunoblotting and GFP fluorescence localization.
Results and discussion
Comparison between constitutive and induced productions of Gap1
The expression of GAP1-GST-6HIS was tested under the regulation of 3 promoters: the constitutive promoter of the plasma membrane H+-ATPase gene (PPMA1), the promoter of the galactokinase GAL1 gene (PGAL1) which is regulated by the carbon source and the natural promoter (PGAP1), an inductive promoter subject to NCR. PPMA1 and PGAL1 have been already used to express membrane proteins [12, 25, 26] but PGAP1 has not. Genes under the regulation of PPMA1 are constitutively expressed regardless of the medium composition. Conversely, genes under the regulation of PGAL1 or PGAP1 are only produced when a minimal medium is used in order to impose a specific carbon source for PGAL1 (galactose) or a specific nitrogen source for PGAP1 (proline).
High level production of Gap1
Purification of Gap1
A detailed purification protocol is described in “Material and Methods” but the determinant factors are discussed in this section. Yeasts are surrounded by a thick cell wall that can be removed by mechanical disruption (glass beads or high pressure homogenizer) or by enzymatic digestion. The latter being quite expensive for large amount of cells, the mechanical approaches were preferred. In particular, the high pressure homogenization (Avestin EmulsiFlex-C3) was chosen for its reproducibility, efficiency and ease of use, as compared to cell disruption using glass beads. As the technique tends to break up vacuoles and causes the release of proteases, a specific cocktail of protease inhibitors (leupeptin, chymostatin, pepstatin, PMSF, and EDTA to inactive metal-dependent proteases) was used to avoid target proteolysis. Typically, 40 to 50 grams of wet cells (corresponding to 1/4 of a bio-reactor) were resuspended in 200 mL of lysis buffer and disrupted in the presence of protease inhibitors. Cells lysate was cleared by low speed centrifugation at 3,000 g and membranes were pelleted at 120,000 g. Solubilization is a crucial step for membrane protein purification. A wide variety of detergents are available to extract the target protein from the membrane and to maintain it in solution while avoiding any irreversible unfolding during the purification. In order to find the most suitable detergent for Gap1 purification, several commonly used detergents were tested: zwitterionic long chain fos-cholines FC14 and FC16, glycosylated short chain octyl- and nonyl-glucosides OG and NG, and glycosylated long chain decyl- and dodecyl- maltopyranoside DM and DDM. Surprisingly, only DDM was able to solubilize and keep the protein migration profile unaffected. All other detergent treatments led to protein degradation and alteration in migration profiles. Pelleted membranes were resuspended in the same buffer but without EDTA and solubilized by addition of DDM (2% final). Insolubilized membranes were pelleted at 120,000 g and the supernatant applied on pre-equilibrated Ni-NTA resin. A critical background concentration of 10 mM of imidazole was used during the purification to avoid non-specific binding to the resin. Based on the SDS-PAGE analysis reported in Figure 3C.1, Gap1 eluted from Ni-NTA resin was almost pure. About 1 milligram of Gap1 was obtained for 1 liter of culture. The purified sample was also subjected to size-exclusion chromatography to measure the monodispersity of the protein (see Additional file 2: Figure S2). We observe a major peak corresponding to the monomeric form of the protein embedded in a detergent micelle. In addition, significant amounts of multimeric forms are present, indicating that further improvements in the purification protocol may be required for applications requiring strictly monodisperse protein (i.e. crystallography). On SDS-PAGE, the purified Gap1 appears as a defined double band and no multimeric forms appear after purification. These forms can be observed in the total protein extract but are either transient or not purified. The double band was previously reported to be due to the phosphorylation of the protein . After alkaline phosphatase treatment on our purified sample, we observe the disappearance of the upper band, confirming that the doublet is due to phosphorylation (see Additional file 3: Figure S3). To assess the integrity of the protein, we have reconstituted Gap1 in a commercial lipid extract of S. cerevisiae and measured the sample by infrared spectroscopy. Spectra obtained by attenuated total reflection infrared spectroscopy (ATR-FTIR) contain bands of absorption of all chemical bounds present in the sample at a wavenumber depending on their chemical environment. This allows to see signature absorption bands of chemical bounds of lipids and proteins and to evaluate secondary structure content of the sample. As can be seen in Figure 3D, our sample contains both signature bands of lipid and protein, and the band of protein has its maximum of absorption at 1655 cm−1, which is typical of α-helix proteins, as expected of a member of the APC family [28, 29]. To our knowledge, it is the first reported expression, purification and reconstitution of Gap1.
Extension of the production protocol to other proteins Table 1
Summary of the proteins expressed during this work
Expected size (kDa)
General amino acid transporter
Cytosolic N-terminus part of Gap1
Lipid-binding protein, LPS co-receptor
Protein quantification by whole cell fluorescence measurements
Expected size (kDa)
(μg per g of cells**)
3325 ± 49
1971 ± 54
4424 ± 18
733 ± 38
16801 ± 514
17914 ± 123
8032 ± 161
3129 ± 32
865 ± 113
4130 ± 66
During this study, we have established a simple and efficient system to produce and purify milligrams of the general amino transporter of yeast S. cerevisiae, such expression and purification has never been reported so far. This system combines high yield, ease of use and low cost of production. To our knowledge, this is also the first time that the NCR is used to control protein production. This efficient and tightly regulated pathway coupled with fairly simple bio-reactor techniques has led us to this new system for protein expression. Such quantities of purified Gap1 allow proceeding with in vitro experiments and envisaging structural biology techniques. Although many studies have deciphered the regulation of the protein, both at the transcription and the protein level [13, 37, 38], little is known about the transport mechanism and the substrate recognition [39, 40]. We expect that this production tool will facilitate in vitro studies and overall understanding of the protein. From this perspective, we have successfully reconstituted the protein in liposomes made of yeast lipids extract which pave the way to transport assays and structural biology experiments.
From a methodological perspective, by combining our system with the well-established GFP reporter [12, 41], we have shown that it can be used to express human proteins, both soluble and inserted in the membrane. Compared to the promoter of PMA1, an inducible promoter such as the promoter of Gap1 seems more relevant for protein overexpression: constitutive overexpression slows cell growth dramatically and in our hands, leads to proteins aggregation. Renewing the medium before expression requires some additional manipulation compared to constitutive expression but allows reaching higher biomass per liter of culture (40 grams versus 8 grams per liter) and can be useful for secreted proteins that are not stable at low pH or are sensitive to yeast byproducts (e.g. ethanol). As Gap1 is not an essential gene and the results presented here were obtained with a centromeric (low copy) plasmid, direct genome integration can be used to avoid plasmid instability, a recurring problem in yeast protein expression, without affecting the number of copy of the gene.
Taken together, our results show that NCR in general and the Gap1 promoter in particular can be used to create a robust, cost-effective and high-throughput expression system in S. cerevisiae that can be used when specific requirements are needed such as a eukaryotic system, membrane integration or difficult protein secretion.
Strains, plasmids and media
All expression vectors were tested in a Σ1278b gap1Δ ura3 background . Cells were either grown in a rich medium (1%(w/v) yeast extract, 1%(w/v) bactopeptone, 2%(w/v) glucose) or in a defined medium (MgSO4 3 mM, KH2PO4 7 mM, CaCl2.2H2O 3 mM, NaCl 9 mM, K2SO4 6 mM, citric acid 50 mM, KOH 160 mM, proline 9 mM, glucose 3%(w/v), pH 6.1, traces of metals and vitamins). Cultures were grown at 30°C and expression induced at 30 or (where specified) 25°C. During expression phases, the medium was supplemented with 10% glycerol as a chemical chaperone . Medium switches were performed by centrifugation at moderate speed (7,000 g during 15 min) and resuspension in inductive medium. Cells were grown either in agitated flasks or in bio-reactor (Sartorius BIOSTAT® A+).
Genes were inserted in a plasmid containing URA3 (yeast selection marker), CEN/ARS (yeast origin of replication), ampR (bacteria selection marker) and ori (bacteria origin of replication). Expression vectors were obtained by in vivo recombination in yeast : genes were amplified by PCR using specific oligonucleotide primers containing 40 bases corresponding to the target vector at their 5′ extremities. The vector (already containing the GAP1 promoter and the CYC1 terminator obtained the same way) was linearized using a specific restriction enzyme (AgeI). Both the linearized vector and the PCR products were transformed in yeast using the lithium acetate technique . Transformants were plated on defined medium supplemented with 1%(m/v) agarose. Colonies generally appeared after 2 days at 30°C. Two to four colonies were cultivated on selective medium and their DNA was extracted using phenol/chloroform technique . The extracted DNA was transformed in bacteria in order to produce sufficient amounts of DNA at required purity to perform sequencing. Confirmed DNA was transformed in expression strain and transformants were saved at −80°C.
Gap1 activity was determined by measuring the initial rate of uptake of 14C- labelled citrulline (20 mM), a specific substrate of the permease . At each expression time point (0, 1, 2 and 4 hours), a known quantity of 14C-citrulline was added to the cells. A small amount of cells was collected and washed after 30, 60 and 90 seconds and the radioactivity was counted for each sample. A linear regression was operated on the three values and the slope was extracted. This slope was normalized by the total quantity of protein and the activity of 14C-citrulline. The resultant protein’s activity was expressed in nmol of 14C-citrulline per minutes and milligrams of proteins. All measurements were done three times and their consistency was verified.
All cultures were grown at 30°C unless otherwise specified. A saturated pre-culture done on minimal proline medium was diluted (100-fold) in a five liter bio-reactor containing rich medium. The bio-reactor (Sartorius Biostat A+) is equipped with a pH probe, an oxygen probe, a level/foam detector, an air injector, a four-way injector, a rotor, an external heating blanket and cooler devices for both exhaust gas and internal medium. All operations were controlled by an external computer and a dedicated software (BIOSTAT Aplus PC Panel μDCU). Foam formation was prevented by addition of antifoam and pH was maintained at 5.5 by addition of 5 M KOH during the process. Oxygen concentration inside the medium was kept above 40% of its initial concentration by increasing the stirring speed. After 24 h, a drop in oxygen consumption was observed and the medium was exchanged by centrifugation (15 min, 7,500 g, Avanti™ J-20 XPI Centrifuge 6 L, Beckman Coulter) with fresh minimal medium (containing 0.3% proline and 3% glucose). Depending on the experiment, minimal medium was supplemented with 10% glycerol to increase protein stability and/or the temperature was lowered to 25°C. The induction time varied from 2 to 24 hours. Cells were then harvested by centrifugation (15 min, 7,500 g) and washed twice in decreasing amount of Tris–HCl (10 mM, pH7.5). After the last centrifugation, cells were frozen at −80°C.
Purification of Gap1
Yeast were resuspended in 5 volumes of lysis buffer (40–50 grams of cells in 200 mL final) containing Tris–HCl pH 7.5 100 mM, NaCl 150 mM, glycerol 10%(m/v), beta-mercapto-ethanol 20 mM, EDTA 10 mM, leupeptin 10 μg/mL, pepstatin 10 μg/mL, chymostatin 2.5 μg/mL and PMSF (phenylmethanesulfonylfluoride) 2.5 mg/mL. Cells were disrupted by homogenization using an Avestin EmulsiFlex C3 (1 passage at low pressure and 3 passages at more than 25,000 psi). Cell debris were removed by low speed centrifugation (15 min at 3,000 g). The supernatant was ultracentrifuged (1 hour at 125,000 g) to pellet the membranes. Membranes were resupended in 50 mL purification buffer containing Tris–HCl pH 7.5 100 mM, NaCl 150 mM, glycerol 10%(m/v), beta-mercapto-ethanol 1 mM, tris(2-carboxyethyl)phosphine (TCEP) 100 μM. Solubilization was achieved by incubation under slow agitation at 4°C with 2%(m/v) DDM (n-dodecyl-beta-D-maltopyranoside). The fraction resistant to detergent was removed by another ultracentrifugation step and the supernatant was applied on Ni-NTA resin. Imidazole (10 mM final) was added to avoid unspecific binding on the column and high contamination of the final sample. Proteins were incubated 1 hour at 4°C with the resin under slow agitation. The resin was washed with 5 Column Volumes (CV) of purification buffer containing 10 mM imidazole and 2x CV containing 20 mM imidazole. Gap1 was eluted with 250 mM imidazole by fraction of 500 μL (5 to 7 CV). The most concentrated fractions were pooled together and tested by SDS-PAGE. Size exclusion chromatography was used to control the dispersity of the purified Gap1. The pooled fractions were loaded on a size exclusion column (SDX-200 10/300GL) and the protein was detected by UV absorption. Molecular weight standards (BioRad) were used to estimate the apparent mass. The phosphorylation was assayed by treating the purified protein with alkaline phosphatase (Roche) according to the manufacturer instructions and Gap1 was revealed using a polyclonal antibody raised against Gap1 .
Reconstitution of Gap1 and infrared spectroscopy
A dried film of yeast lipid extract (2 mg) (Avanti Polar Lipids, Inc. - Yeast Total Lipid Extract) was obtained by evaporation of chloroform under a flow of nitrogen, followed by overnight drying under vacuum. Liposomes were prepared by sonication of the lipid film for 3 × 1 min on a 250 W Vibra Cell Sonifier in 300 μL Tris–HCl pH 7.5 20 mM, NaCl 75 mM. The purified Gap1 in the presence of 0.5% DDM was mixed with liposomes at a protein to lipid ratio of 1:50 w/w and incubated for 30 min at 4°C under gentle agitation. The detergent was then removed by absorption on SM2 Bio-Beads (four incubations of respectively: one hour, overnight and twice one hour under agitation in the presence of 40 mg Bio-Beads).
Infrared spectroscopy spectra were taken using Attenuated Total Reflection-Fourier Transform Infrared spectroscopy (ATR-FTIR) . ATR-FTIR spectra were recorded at room temperature on a Equinox 55 infrared spectrophotometer (Bruker Optics) equipped with a Golden Gate reflectance accessory (Specac) at a nominal resolution of 2 cm−1 and encoded every 1 cm−1. The spectrophotometer was continuously purged with air dried on a FTIR purge gas generator 75 – 62 Balston (Maidstone, UK) at a flow rate of 5.8 L/min. The internal reflection element was a diamond crystal (2 mm × 2 mm) with an aperture angle of 45° that yielded a single internal reflection. Samples were prepared by spreading 2 μl of the proteoliposomes suspension on the diamond crystal surface and by removing the excess water under nitrogen flow. The signal from the atmospheric water was subtracted as described by Goormaghtigh and Ruysschaert . The data presented here are the average of 128 spectra to improve the signal/noise ratio. Data were processed using “Kinetics”, an analysis program developed in our laboratory and running under MatLab (The MathWorks, Natick, MA).
SDS-PAGE and immuno-blotting
Whole cell lysates (2 mL at OD660 0.5) or purified proteins (30 μL at a protein concentration of 0.3 mg/mL) were analyzed by standard SDS-PAGE using polyacrylamide gels (Mini-PROTEAN® TGX™ Precast Gels, Bio-Rad Laboratories N.V.) followed either a Coomassie staining or a transfer to nitrocellulose membrane (Bio-Rad Laboratories N.V.) for immuno-blotting. Poly-histidines tags were detected using the QIAexpress® Anti-his Hrp Conjugate Kit (Qiagen) and GFP tags were detected using anti-GFP Rabbit IgG Polyclonal Antibody Fraction (Molecular Probes®). Proteins were visualized by electro-chemiluminescence using the Luminata™ Forte Western Hrp Substrate (Merck Millipore) and pictures were taken using the ECL-system ImageQuant 400® from GE Healthcare. Images were layered and cropped using Photoshop (Adobe).
GFP imaging was done using a microscope Axio Scope.A1 (Zeiss) with an objective 100X. 2 μL of a suspension of cells at OD660 1 were spread on a glass slide and images were taken at room temperature without any kind of fixing. Images were taken using the Zeiss software (Axio Vision 4.8.2). Images were cropped using Photoshop (Adobe).
The expression of MD2, N-ter Gap1, Uga4, Gap1 and Vglut1 was evaluated by GFP quantification. A protocol analog to the one described by Drew, et al. was used to quantify the expression. The GFP intensity of a known quantity of cells transformed with the corresponding expression vector and cultivated on inductive medium was measured and reported to the standard curve. A standard curve was established using successive dilutions of purified GFP, a 6-fold intensity factor was applied in order to take into account the fluorescence yield difference between wt GFP (used for the standard curve) vs. S65T GFP (present in the chimeric constructs) . By taking into account the molecular weight of each proteins, we can estimate of the quantity produced for 40 grams of wet weight cells (a typical yield for one liter of culture in fermenter).
This work was supported by the “ARC – Actions de Recherche Concertées” grant (to BA and CG) and a Mandat d’Impulsion Scientifique (n° F.4523.12) from the Fonds de la Recherche Scientifique (F.R.S.-F.N.R.S.), Belgium to CG. FD was a fellow of the FRIA. CG is a Chercheur Qualifié of the FNRS. The authors would first like to thank Dr Patrick Downey and Dr Florence Lebon from UCB Pharma, UCB NewMedicines for providing the VGLUT1 optimized gene. The authors would also like to thank Catherine Jauniaux and Lydia Spedale for their technical expertise and logistical support; Anastassia Troupiotis-Tsaïlaki for her help with infrared spectroscopy measurements and Jonathan Ghesquière and Alexandra Gonzalez Garcia for manuscript reviewing.
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