Heterologous expression and purification of the cystic fibrosis transmembrane conductance regulator (CFTR) are significant challenges and limiting factors in the development of drug therapies for cystic fibrosis. This protocol describes two methods for the isolation of milligram quantities of CFTR suitable for functional and structural studies.
Defects in the cystic fibrosis transmembrane conductance regulator (CFTR) protein cause cystic fibrosis (CF), an autosomal recessive disease that currently limits the average life expectancy of sufferers to <40 years of age. The development of novel drug molecules to restore the activity of CFTR is an important goal in the treatment CF, and the isolation of functionally active CFTR is a useful step towards achieving this goal.
We describe two methods for the purification of CFTR from a eukaryotic heterologous expression system, S. cerevisiae. Like prokaryotic systems, S. cerevisiae can be rapidly grown in the lab at low cost, but can also traffic and posttranslationally modify large membrane proteins. The selection of detergents for solubilization and purification is a critical step in the purification of any membrane protein. Having screened for the solubility of CFTR in several detergents, we have chosen two contrasting detergents for use in the purification that allow the final CFTR preparation to be tailored to the subsequently planned experiments.
In this method, we provide comparison of the purification of CFTR in dodecyl-β-D-maltoside (DDM) and 1-tetradecanoyl-sn-glycero-3-phospho-(1'-rac-glycerol) (LPG-14). Protein purified in DDM by this method shows ATPase activity in functional assays. Protein purified in LPG-14 shows high purity and yield, can be employed to study post-translational modifications, and can be used for structural methods such as small-angle X-ray scattering and electron microscopy. However it displays significantly lower ATPase activity.
Cystic fibrosis (CF) is the most common genetic disorder in Europe and North America with an incidence of about 1 in 2,500 live births. CF occurs when mutations in the cystic fibrosis transmembrane conductance regulator (CFTR) protein cause loss of its function at the plasma membrane of epithelial cells1. The most serious consequence of this defect is irreversible lung damage, which shortens the life expectancy of sufferers to <40 years of age2,3.
CFTR is an ATP-binding cassette (ABC) transporter that has evolved to become an ion channel1,4. Despite its quite altered function in the plasma membrane of cells, it still retains significant sequence homology with other ABC transporters. Intriguingly, the specialized parts of CFTR (i.e. its regulatory region and its N- and C-termini) share no significant sequence similarity with other metazoan ABC transporters, hence there are no clues as to the origins of these sequences in CFTR. On the basis of its primary structure, CFTR is classified as a C-family member of the ABC transporter family, but there is no strong evidence for a residual functional linkage to this sub-family. There have been some reports of glutathione transport activity for CFTR5-7, which would be consistent with the roles of other C-family members8,9, although other reports suggest that reduced glutathione may inhibit the CFTR ATPase activity, rather than showing the substrate-induced stimulation that characterize the ABC transporters10. Measurement of ion conductance is sufficiently sensitive to allow the channel activity of single CFTR molecules to be studied1 and CFTR channel properties have been monitored as a function of time, temperature, ATP concentration, membrane potential, and phosphorylation state, as well as in the presence of a host of small molecule inhibitors, potentiators, and modifiers. These studies have also added significantly to our knowledge of how ABC transporters function. Nevertheless, expression of CFTR in significant amounts and its subsequent purification has proven to be particularly challenging and success has been limited to a few laboratories10-13.
The need to develop more effective drugs is pressing, yet this process has been hindered by the lack of purified CFTR for screening small molecules. Solving the CFTR expression and purification problem would enable high-throughput drug screening aimed at correcting the primary defect in CF and would also open up a route for high-resolution structural studies to inform rational drug design. Moreover, even relatively basic biochemical characteristics of the protein, such as its functional oligomeric state, interacting proteins and ATPase activity remain poorly characterized. We have previously reported a protocol for the large-scale expression of GFP- and His-tagged murine CFTR in S. cerevisiae14 and now further describe protocols for the purification of CFTR. We have used these methods to purify five orthologues of CFTR, and present data for the purification of chicken CFTR as an example. The selection of detergents for solubilization and purification is a critical step in the purification of any membrane protein. Having screened for the solubility of CFTR in several detergents, we have chosen two contrasting detergents for use in the purification. Dodecyl-β-D-maltoside (DDM) is a nonionic detergent that has been extensively used for both structural and functional studies of membrane proteins15-21. The ionic detergent 1-tetradecanoyl-sn-glycero-3-phospho-(1'-rac-glycerol) (LPG-14) is highly efficient in the solubilization of CFTR and has previously been used in the purification of functional membrane proteins10,22,23, including purification of CFTR from S. cerevisiae24.
1. Preparation of Buffers
2. Isolation of Yeast Microsomes
3. Solubilization of Microsomes
4. Nickel-affinity Purification of CFTR
5. Gel Permeation Chromatography (GPC) Purification of CFTR
6. Reconstitution of CFTR
7. Measurement of ATPase Activity
The protocol described above is an efficient means to isolate CFTR-enriched microsomes, with almost complete recovery of CFTR during the cell breakage and preparation of the crude microsomes (Figure 1). Other cell breakage methods may also be employed effectively. We have utilized a French pressure cell, and other high-pressure/cavitation devices (also in combination with impacting against a ruby target) with equal efficiency. For convenience and low initial cost of the equipment, we find the bead-beating method the best.
Using LPG to solubilize and purify CFTR yielded 80 μg protein/L culture at >90% purity (Figure 2). The high yield was due to efficient solubilization of CFTR by LPG (compare Figure 2b, lanes 2 and 4). In addition, efficient and tight binding to the column resulted in minimal loss of CFTR in the unbound fraction and the absence of CFTR in the wash fractions (Figure 2, lanes 3, 5, and 6). The eluted protein had a purity of >90%, estimated by Coomassie-stained SDS-PAGE gels and using densitometry of the CFTR and contaminant bands. Gel permeation chromatography (GPC) separated LPG-purified CFTR from low-molecular weight contaminants (Figure 4, lower panel).
The protocol for CFTR purification using DDM gives purity of about 60% and yield of roughly 50 μg/L (Figure 3). Electron microscopy (EM) of negatively stained fractions from the GPC eluting at about 10 ml (Figure 4) showed that DDM-purified CFTR contains aggregates of 20-30 nm diameter as well as smaller particles of 10 nm diameter (data not shown). It is possible that the small aggregates can reversibly associate and dissociate as ultrafiltration with a 1 MDa cut-off filter failed to remove the EM-detectable aggregates. LPG-purified material did not adsorb to a glow-discharged grid, hence was studied by cryo-EM of unstained fractions. This showed a very homogeneous particle population of a relatively small size (6-8 nm diameter, data not shown).
Finally, the ATPase activity of the purified proteins was measured (Figure 5). As a member of the ABC protein family, CFTR has two nucleotide-binding domains (NBDs) capable of binding and/or hydrolyzing ATP. The data indicate that the purified protein was not able to hydrolyze ATP in the LPG-solubilized state and showed weak ATPase activity in the presence of DDM (Figure 5, unfilled bars). After the addition of lipids, and detergent removal, ATPase activity was 4-fold higher for samples that had been purified in DDM (13 nmol ATP/min/mg protein). The addition of lipids and removal of LPG similarly restored activity to CFTR that had been isolated using LPG, but with a final lower rate (1.5 nmol ATP/min/mg protein) than the DDM-purified and reconstituted material.
Figure 1. Monitoring levels of chicken CFTR in cell lysate (CL), supernatants (S) and pellets (P) during various centrifugation steps used for microsome isolation and washing. SDS-PAGE gels were visualized using the in-gel fluorescence of the GFP tag. The supernatant after cell breakage and centrifugation at 14,000 x g contains virtually all the CFTR (including degradation products). Ultracentrifugation at 200,000 x g sediments all the full-length CFTR leaving some fragments in the supernatant. Ultracentrifugation at 100,000 x g of salt-washed microsomes pellets nearly all the CFTR with the removal of some further fragments.
Figure 2. Purification of chicken CFTR in LPG by immobilized metal ion affinity chromatography. Fractions were analyzed by SDS-PAGE followed by Coomassie staining (upper panel) and fluorescence detection of the GFP tag (lower panel). Tracks: (1) Microsomes. (2) LPG-solubilized microsomes. (3) Unbound material. (4) Insoluble material. (5) & (6) 40 and 100 mM imidazole washes. (7) Material eluted with 400 mM imidazole.
Figure 3. Purification of chicken CFTR in DDM by immobilized metal ion affinity chromatography. Fractions were analyzed by SDS-PAGE followed by Coomassie staining. The left hand panel shows fractions prior to elution. Several consecutive elution fractions are shown in the right hand panel with CFTR indicated by the arrow. Later fractions are enriched in a 40 kDa contaminant, which has been identified by mass spectrometry as ribosomal protein L3.
Figure 4. Purification of chicken CFTR by gel permeation chromatography. CFTR purified by Ni-affinity chromatography was concentrated and applied to a GPC column. The elution profile for CFTR (upper panel) purified in buffer containing LPG-14 (solid line) or DDM (dashed line) are overlaid. SDS-PAGE (lower panel) revealed that CFTR eluted between 8 and 11 ml.
Figure 5. ATPase activity of purified chicken CFTR fractions. Protein purified in DDM or LPG was assayed using a modified Chifflet assay26 in the presence of a cocktail of ATPase inhibitors to eliminate any background ATPase activity from F-, P- and V-type ATPases (unfilled bars). The rate of ATP hydrolysis was also measured after detergent removal and lipid addition (filled bars). The plot shows the mean and standard deviation (n=3). Differences between mean values for ATPase activity in presence and absence of lipid, and difference between activity in DDM and LPG are significant to p<0.05.
We have previously described a method for the overexpression of murine CFTR14. Since the publication of that protocol, we have expressed and purified several different orthologs of CFTR using the same system. All orthologs tested so far purified well in the LPG detergent, whilst the DDM purification showed more variation across different orthologs (data not shown). This flexibility illustrates the strength of the yeast approach: it is possible to screen many constructs with relative rapidity in order to select one for a particular purpose.
Washing the yeast microsomes with buffer containing 1 M NaCl prior to solubilization with DDM results in a cleaner microsome preparation and reduces contaminants at later stages. This step is unnecessary in the LPG protocol as the final CFTR sample is >90% pure without the microsome wash. Furthermore, purification in DDM requires several alterations to the buffers for solubilization and purification, namely the addition of extra glycerol and salt. Together, these additions considerably increased the binding of the DDM-solubilized protein to the column.
The DDM purification methodology has scope for improvement, in particular the removal of a 40 kDa major contaminant that, judged by mass spectrometry, is due to the yeast ribosomal subunit L3, which appears to have an inherent affinity for the nickel resin. There is no obvious polyHis sequence in the L3 protein, but examination of its 3D structure when bound to the ribosome (PDB = 1FFK) shows that the folded L3 subunit has a potential polyHis cluster. That this band is less problematic in LPG-purified material may be due to the harsher LPG detergent.
Though the purification in DDM appears to be poorer than that in LPG, milder detergents such as DDM may be more compatible with functional and structural analyses and have already been used in several X-ray crystallographic studies of membrane proteins15-21. Furthermore, our results indicated that the use of LPG leads to loss of ATPase function in CFTR relative to purification in DDM. Hence we would recommend the LPG-based purification protocol for the generation of CFTR where the purity is crucial, for example in applications such as the characterization of post-translational modifications, or in the generation of antibodies, the LPG-based protocol would be chosen. On the other hand in applications where the activity and fully native state of the protein is essential, we would propose the DDM-based protocol as a better option.
To conclude, this protocol describes a reproducible method for the isolation of CFTR in the zwitterionic detergent LPG-14 or the non-ionic detergent DDM. As such it indicates a greater range of purification conditions for CFTR than have previously been reported10-13. In addition milligram quantities of purified CFTR can be obtained using these procedures when combined with a high volume yeast growth system such as a 20 L fermenter and a high capacity cell harvesting system such as a 6 L low speed centrifuge rotor. The CFTR obtained has a cleavable GFP tag which allows easy monitoring of the protein in various biochemical and biophysical assays.
The reagent described in this manuscript (chicken CFTR–containing plasmid or frozen yeast cells) can be obtained through the Cystic Fibrosis Foundation (USA).
The authors have nothing to disclose.
This work was funded by the US Cystic Fibrosis Foundation (CFF) through its CFTR 3D Structure Consortium. TR was funded by a UK CF Trust studentship, and NC by a UK BBSRC studentship. We acknowledge our colleagues in the CFF CFTR 3D structure consortium for their help and advice and for the design of the codon-optimized chicken CFTR sequence and purification tags.
Name of Material/ Equipment | Company | Catalog Number |
0.2μM syringe filter | Sartorius | FC121 |
100 kDa MWCO centrifugal concentrator (PES membrane) | Vivaspin | VS0641 |
2ml microfuge tubes | Sarstedt | 72.695 |
40Ti rotor | Beckman Coulter | 337901 |
50ml Sterile Falcon Tubes | Sarstedt | 62.547.254 |
Adenosine triphosphate disodium salt (Na2ATP) | Sigma-Aldrich | A26209 |
Liquid chromatography system | GE Healthcare | 28-4062-64 |
Aminoethylbenzenesulfonyl fluoride (AEBSF) | Sigma-Aldrich | A8456 |
Glass bead-beating cell disrupter | BioSpec | 1107900 |
Benchtop centrifuge | HERMLE | Z300 |
Benchtop centrifuge | Eppendorf | 5417R |
Benchtop microfuge | Fisher | 13-100-511 |
Benzamidine hydrochloride | Sigma-Aldrich | 434760 |
Hydrophobic Beads SM-2 Adsorbent | BioRad | 152-3920 |
Bromophenol blue | Sigma-Aldrich | 114391 |
Centrifuge tubes | Beckman Coulter | 357000 |
Gel imaging system | BioRad | 170-808 |
Cholesterol | Sigma-Aldrich | C8667 |
Chymostatin | Sigma-Aldrich | C7268 |
Dimethylsulfoxide (DMSO) | Sigma-Aldrich | D8418 |
Dithiothreitol (DTT) | Sigma-Aldrich | 43815 |
E.coli total lipid extract | Avanti lipids | 100500 |
Epoxysuccinyl-leucylamido-butane (E-64) | Sigma-Aldrich | E3132 |
Glass beads, acid washed | Sigma | G8772 |
Glycerol | Fisher | 65017 |
HisTrap HP columns (5 ml) | GE Healthcare | 17-5247-05 |
Rapid Coomassie Stain | Novexin | ISB1L |
Centrifuge JA-17 rotor | Beckman Coulter | 369691 |
Leupeptin | Merck | 108975 |
Lyso-phosphatidyl glycerol-14 (LPG) | Avanti lipids | 858120 |
MgSO4 | Sigma-Aldrich | M7506 |
Gel tank SDS-PAGE system | BioRad | 165-8006 |
n-dodecyl-β-D-maltopyranoside (DDM) | Affymetrix | D310S |
NaCl | Sigma-Aldrich | S6191 |
NaN3 | Sigma-Aldrich | S2002 |
NH4Cl | Sigma-Aldrich | A9434 |
Oligomycin | Sigma-Aldrich | 75351 |
Ultracentrifuge | Beckman Coulter | 392050 |
Prestained protein standards | Fermentas | SM1811 |
Desalting columns (Sephadex G-25) | GE Healthcare | 17-0851-01 |
Pepstatin A | Sigma-Aldrich | P4265 |
Phenylmethanesulfonylfluoride (PMSF) | Sigma-Aldrich | P7626 |
Sch28080 | Sigma-Aldrich | S4443 |
Sodium dodecyl sulfate (SDS) | Sigma-Aldrich | L37771 |
Sodium thiocyanate (NaSCN) | Sigma-Aldrich | 251410 |
Gel filtration 10/300 GL column | GE Healthcare | 17-5172-01 |
Tris-base | Formedium | TRIS01 |
Ultracentrifuge tubes | Beckman Coulter | 355618 |
Vortex mixer | Star Labs | N2400-0001 |
Ultrasonic water bath | Ultrawave | F0002202 |
Multimode plate reader | BioTek | BTH1MF |