Small-scale, semi-automated purification of eukaryotic proteins for structure determination

A simple approach that allows cost-effective automated purification of recombinant proteins in levels sufficient for functional characterization or structural studies is described. Studies with four human stem cell proteins, an engineered version of green fluorescent protein, and other proteins are included. The method combines an expression vector (pVP62K) that provides in vivo cleavage of an initial fusion protein, a factorial designed auto-induction medium that improves the performance of small-scale production, and rapid, automated metal affinity purification of His8-tagged proteins. For initial small-scale production screening, single colony transformants were grown overnight in 0.4 ml of auto-induction medium, produced proteins were purified using the Promega Maxwell 16, and purification results were analyzed by Caliper LC90 capillary electrophoresis. The yield of purified [U-15N]-His8-Tcl-1 was 7.5 microg/ml of culture medium, of purified [U-15N]-His8-GFP was 68 microg/ml, and of purified selenomethione-labeled AIA-GFP (His8 removed by treatment with TEV protease) was 172 microg/ml. The yield information obtained from a successful automated purification from 0.4 ml was used to inform the decision to scale-up for a second meso-scale (10-50 ml) cell growth and automated purification. 1H-15N NMR HSQC spectra of His8-Tcl-1 and of His8-GFP prepared from 50 ml cultures showed excellent chemical shift dispersion, consistent with well folded states in solution suitable for structure determination. Moreover, AIA-GFP obtained by proteolytic removal of the His8 tag was subjected to crystallization screening, and yielded crystals under several conditions. Single crystals were subsequently produced and optimized by the hanging drop method. The structure was solved by molecular replacement at a resolution of 1.7 A. This approach provides an efficient way to carry out several key target screening steps that are essential for successful operation of proteomics pipelines with eukaryotic proteins: examination of total expression, determination of proteolysis of fusion tags, quantification of the yield of purified protein, and suitability for structure determination.     

A General Bacterial Expression System for Functional Analysis of cDNA-Encoded Proteins

A general system for functional analysis of cDNA-encoded proteins is described. The basic concept involves the expression inEscherichia coliof selected portions of cDNAs in an approach toward the understanding of the function of the corresponding proteins. A selected cDNA is expressed as part of a fusion protein used for immunization to elicit antibodies, and a corresponding fusion protein, having the cDNA-encoded portion in common, for purification of target protein-specific antibodies. This antiserum could be used for functional analysis of the cDNA-encoded protein, e.g., by immunohistology. Two general expression vector systems forE. colihave been constructed, both (i) designed with multiple cloning sites in three different reading frames, (ii) having their protein production controlled by the tightly regulated T7 promoter, and (iii) enabling affinity purification of the expressed target proteins by fusions to IgG-binding domains derived from staphylococcal protein A or a serum albumin-binding protein derived from streptococcal protein G, respectively. This novel system has been evaluated by expressing five cDNAs, isolated from pre- pubertal mouse testis by a differential cDNA library screening strategy. All five clones could be expressed intracellularly inE. colias fusion proteins with high production levels, ranging from 4 to 500 mg/liter, and affinity purification yielded essentially full-length products. Characterization of affinity-purified antibodies revealed that there exists no cross-reactivity between the two fusion systems and that such antibodies indeed could be used for immunohistology. The implications for the described system for large-scale functional analysis of cDNA libraries are discussed.     

An automated small-scale protein expression and purification screening provides beneficial information for protein production

One of the first key steps in structural genomics is high-throughput expression and rapid screening to select highly soluble proteins, the preferred candidates for crystal production. Here we describe the methodology used at the Berkeley Structural Genomics Center (BSGC) for automated parallel expression and small-scale purification of fusion proteins using a 96-well format. Our robotic method includes cell lysis, soluble fraction separation and purification with affinity resins. For detection of His-tagged proteins in the soluble fractions and after affinity resin elution, a dot-blot procedure with an anti-His-antibody is used. The expression level and molecular mass of recombinant proteins are checked by SDS-PAGE. With this approach, we are able to obtain beneficial information to be used for large-scale protein expression and purification.     

High-throughput purification of recombinant proteins using self-cleaving intein tags

High throughput methods for recombinant protein production using E. coli typically involve the use of affinity tags for simple purification of the protein of interest. One drawback of these techniques is the occasional need for tag removal before study, which can be hard to predict. In this work, we demonstrate two high throughput purification methods for untagged protein targets based on simple and cost-effective self-cleaving intein tags. Two model proteins, E. coli beta-galactosidase (βGal) and superfolder green fluorescent protein (sfGFP), were purified using self-cleaving versions of the conventional chitin-binding domain (CBD) affinity tag and the nonchromatographic elastin-like-polypeptide (ELP) precipitation tag in a 96-well filter plate format. Initial tests with shake flask cultures confirmed that the intein purification scheme could be scaled down, with >90% pure product generated in a single step using both methods. The scheme was then validated in a high throughput expression platform using 24-well plate cultures followed by purification in 96-well plates. For both tags and with both target proteins, the purified product was consistently obtained in a single-step, with low well-to-well and plate-to-plate variability. This simple method thus allows the reproducible production of highly pure untagged recombinant proteins in a convenient microtiter plate format.     

Expression and purification of a novel mannose-binding lectin from Pinellia ternata

Pinellia ternata agglutinin (PTA) from the tubers of P. ternata is a monocot mannose-binding lectin that catalytically agglutinated rabbit erythrocytes. The potential effect of PTA has gained considerable interest in recent years owing to clinical use of native PTA as the preparation against cancer and for plant protection against insect pests. Here we report a successful strategy to allow high-level expression of PTA as inclusion bodies in Escherichia coli M15. Purification of refolded recombinant protein from solubilized inclusion bodies by Ni-NTA agarose affinity chromatography yielded biological activity recombinant PTA (final yield of about 10 mg/L). The recombinant PTA agglutinated rabbit erythrocytes to a dilution similar to that determined for “native” lectin purified from P. ternata. The expression and purification system makes it possible to obtain sufficient quantities of biologically active and homogenous recombinant PTA sufficient to carry out advanced clinical trials. This is the first report on the large-scale expression and purification of biologically active recombinant PTA from E. coli.     

High quality protein microarray using in situ protein purification

Background  

In the postgenomic era, high throughput protein expression and protein microarray technologies have progressed markedly permitting screening of therapeutic reagents and discovery of novel protein functions. Hexa-histidine is one of the most commonly used fusion tags for protein expression due to its small size and convenient purification via immobilized metal ion affinity chromatography (IMAC). This purification process has been adapted to the protein microarray format, but the quality of in situ His-tagged protein purification on slides has not been systematically evaluated. We established methods to determine the level of purification of such proteins on metal chelate-modified slide surfaces. Optimized in situ purification of His-tagged recombinant proteins has the potential to become the new gold standard for cost-effective generation of high-quality and high-density protein microarrays.     

The Center for Optimized Structural Studies (COSS) platform for automation in cloning,expression, and purification of single proteins and protein–protein complexes

Expression in Escherichia coli represents the simplest and most cost effective means for the production of recombinant proteins. This is a routine task in structural biology and biochemistry where milligrams of the target protein are required in high purity and monodispersity. To achieve these criteria, the user often needs to screen several constructs in different expression and purification conditions in parallel. We describe a pipeline, implemented in the Center for Optimized Structural Studies, that enables the systematic screening of expression and purification conditions for recombinant proteins and relies on a series of logical decisions. We first use bioinformatics tools to design a series of protein fragments, which we clone in parallel, and subsequently screen in small scale for optimal expression and purification conditions. Based on a scoring system that assesses soluble expression, we then select the top ranking targets for large-scale purification. In the establishment of our pipeline, emphasis was put on streamlining the processes such that it can be easily but not necessarily automatized. In a typical run of about 2 weeks, we are able to prepare and perform small-scale expression screens for 20–100 different constructs followed by large-scale purification of at least 4–6 proteins. The major advantage of our approach is its flexibility, which allows for easy adoption, either partially or entirely, by any average hypothesis driven laboratory in a manual or robot-assisted manner.     

Optimized E. coli expression strain LOBSTR eliminates common contaminants from His‐tag purification

His‐tag affinity purification is one of the most commonly used methods to purify recombinant proteins expressed in E. coli. One drawback of using the His‐tag is the co‐purification of contaminating histidine‐rich E. coli proteins. We engineered a new E. coli expression strain, LOBSTR (lo w b ackground str ain), which eliminates the most abundant contaminants. LOBSTR is derived from the E. coli BL21(DE3) strain and carries genomically modified copies of arnA and slyD, whose protein products exhibit reduced affinities to Ni and Co resins, resulting in a much higher purity of the target protein. The use of LOBSTR enables the pursuit of challenging low‐expressing protein targets by reducing background contamination with no additional purification steps, materials, or costs, and thus pushes the limits of standard His‐tag purifications. Proteins 2013; 81:1857–1861. © 2013 Wiley Periodicals, Inc.     

Purification of recombinant protein by cold‐coacervation of fusion constructs incorporating resilin‐inspired polypeptides

Polypeptides containing between 4 and 32 repeats of a resilin‐inspired sequence AQTPSSYGAP, derived from the mosquito Anopheles gambiae, have been used as tags on recombinant fusion proteins. These repeating polypeptides were inspired by the repeating structures that are found in resilins and sequence‐related proteins from various insects. Unexpectedly, an aqueous solution of a recombinant resilin protein displays an upper critical solution temperature (cold‐coacervation) when held on ice, leading to a separation into a protein rich phase, typically exceeding 200 mg/mL, and a protein‐poor phase. We show that purification of recombinant proteins by cold‐coacervation can be performed when engineered as a fusion partner to a resilin‐inspired repeat sequence. In this study, we demonstrate the process by the recombinant expression and purification of enhanced Green fluorescent protein (EGFP) in E. coli. This facile purification system can produce high purity, concentrated protein solutions without the need for affinity chromatography or other time‐consuming or expensive purification steps, and that it can be used with other bulk purification steps such as low concentration ammonium sulfate precipitation. Protein purification by cold‐coacervation also minimizes the exposure of the target protein to enhanced proteolysis at higher temperature. Biotechnol. Bioeng. 2012; 109: 2947–2954. © 2012 Wiley Periodicals, Inc.     

Synthesis, purification and bioactivity of recombinant human activin A expressed in the yeast Pichia pastoris

The transforming growth factor-beta (TGF-β) superfamily member, activin A, plays a central role in the regulation of multiple physiological processes including cell differentiation, mitogenesis, embryogenesis, apoptosis and inflammation. In normal cells, activin A signalling is regulated to maintain cellular and tissue health and suppress tumour growth. Disruption of activin A signalling has been implicated in tumour formation and progression. Hence, the availability of activin A is an important target for the development of diagnostics and drugs for therapeutic intervention. To this end, we have expressed human activin A in Pichia pastoris, permitting its secretion into culture medium and purification as the mature homodimer. A construct was engineered encoding the monomeric precursor protein with a N-terminal FLAG affinity tag (DYKDDDDK) and a cleavage site (EKR) for Kex2p protease. Procedures for the two-step purification of human activin A by ion-exchange and anti-FLAG antibody affinity chromatography, and for the removal of the FLAG affinity tag from purified recombinant human activin A by enteropeptidase, are described. The molecular weights of the FLAG-tagged and de-tagged human activin A were confirmed by MALDI-TOF mass spectroscopy. The biological activity of these recombinant activins was assessed for their effects on modulating the secretion of Endothelin-1 (ET-1) by human umbilical vein endothelial cells (HUVECs). The recombinant human activin A containing the intact FLAG tag resulted in a reduced ET-1 secretion from HUVECs, whereas upon removal of this affinity purification tag the purified recombinant human activin A restored ET-1 secretion to levels comparable to the positive control. These results document an approach of considerable potential for the simple, large-scale expression and purification of this important human growth factor for use in diagnostic and therapeutic purposes.     

The novel Fh8 and H fusion partners for soluble protein expression in Escherichia coli: a comparison with the traditional gene fusion technology

The Escherichia coli host system is an advantageous choice for simple and inexpensive recombinant protein production but it still presents bottlenecks at expressing soluble proteins from other organisms. Several efforts have been taken to overcome E. coli limitations, including the use of fusion partners that improve protein expression and solubility. New fusion technologies are emerging to complement the traditional solutions. This work evaluates two novel fusion partners, the Fh8 tag (8 kDa) and the H tag (1 kDa), as solubility enhancing tags in E. coli and their comparison to commonly used fusion partners. A broad range comparison was conducted in a small-scale screening and subsequently scaled-up. Six difficult-to-express target proteins (RVS167, SPO14, YPK1, YPK2, Frutalin and CP12) were fused to eight fusion tags (His, Trx, GST, MBP, NusA, SUMO, H and Fh8). The resulting protein expression and solubility levels were evaluated by sodium dodecyl sulfate polyacrylamide gel electrophoresis before and after protein purification and after tag removal. The Fh8 partner improved protein expression and solubility as the well-known Trx, NusA or MBP fusion partners. The H partner did not function as a solubility tag. Cleaved proteins from Fh8 fusions were soluble and obtained in similar or higher amounts than proteins from the cleavage of other partners as Trx, NusA or MBP. The Fh8 fusion tag therefore acts as an effective solubility enhancer, and its low molecular weight potentially gives it an advantage over larger solubility tags by offering a more reliable assessment of the target protein solubility when expressed as a fusion protein.     

Growth and recombinant protein expression with <Emphasis Type="Italic">Escherichia coli</Emphasis> in different batch cultivation media

Parallel operated milliliter-scale stirred tank bioreactors were applied for recombinant protein expression studies in simple batch experiments without pH titration. An enzymatic glucose release system (EnBase), a complex medium, and the frequently used LB and TB media were compared with regard to growth of Escherichia coli and recombinant protein expression (alcohol dehydrogenase (ADH) from Lactobacillus brevis and formate dehydrogenase (FDH) from Candida boidinii). Dissolved oxygen and pH were recorded online, optical densities were measured at-line, and the activities of ADH and FDH were analyzed offline. Best growth was observed in a complex medium with maximum dry cell weight concentrations of 14 g L⁻¹. EnBase cultivations enabled final dry cell weight concentrations between 6 and 8 g L⁻¹. The pH remained nearly constant in EnBase cultivations due to the continuous glucose release, showing the usefulness of this glucose release system especially for pH-sensitive bioprocesses. Cell-specific enzyme activities varied considerably depending on the different media used. Maximum specific ADH activities were measured with the complex medium, 6 h after induction with IPTG, whereas the highest specific FDH activities were achieved with the EnBase medium at low glucose release profiles 24 h after induction. Hence, depending on the recombinant protein, different medium compositions, times for induction, and times for cell harvest have to be evaluated to achieve efficient expression of recombinant proteins in E. coli. A rapid experimental evaluation can easily be performed with parallel batch operated small-scale stirred tank bioreactors.     

InsectDirectTM System: Rapid, High-level Protein Expression and Purification from Insect Cells

A fundamental challenge in high-throughput (HT) expression screening is to rapidly identify the appropriate expression system for many targets in parallel. Known or unknown open reading frames (ORFs) are typically amplified by PCR and then cloned into a variety of vectors, producing recombinants used to direct target protein expression in Escherichia coli, insect cells, mammalian cells, or yeast. To facilitate rapid expression and purification in Spodoptera insect cells (Sf9), we developed transient expression vectors that include an enterokinase cleavage site immediately upstream of a ligation-independent cloning site (Ek/LIC). We also developed a high-efficiency insect cell transfection reagent, and automation-compatible fusion protein purification system for insect cells to facilitate expression screening and protein production. Positive clones identified from the small-scale screening were subjected to a larger scale production. Using this InsectDirect^TM approach, we successfully expressed milligram quantities of different human proteins including heat shock proteins, phospholipases, and protein kinases.     

Cloning, expression and purification of extracellular serine protease Esp, a biofilm-degrading enzyme, from Staphylococcus epidermidis

Aims: Staphylococcus epidermidis Esp, an extracellular serine protease, inhibits Staphylococcus aureus biofilm formation and nasal colonization. To further expand the biotechnological applications of Esp, we developed a highly efficient and economic method for the purification of recombinant Esp based on a Brevibacillus choshinensis expression–secretion system. Methods and Results: The esp gene was fused with the N‐terminal Sec‐dependent signal sequence of the B. choshinensis cell wall protein and a C‐terminal hexa‐histidine‐tag gene. The recombinant Esp was expressed and secreted into the optimized medium as an immature form and subsequently activated by thermolysin. The mature Esp was easily purified by a single purification step using nickel affinity chromatography and showed proteolytic activity as well as Staph. aureus biofilm destruction activity. Conclusions: The purification yield of the developed extracellular production system was 5 mg recombinant mature Esp per 20‐ml culture, which was much higher than that of an intracellular production system in Escherichia coli (3 mg recombinant Esp per 1‐l culture). Significance and Impact of the Study: Our findings will be a powerful tool for the production and purification of recombinant Esp and also applicable to a large variety of recombinant proteins used for basic researches and biotechnological applications.     

Heterologous expression of the <Emphasis Type="Italic">msp2 gene</Emphasis> from <Emphasis Type="Italic">Marasmius scorodonius</Emphasis>

For the heterologous expression of the msp2 gene from the edible mushroom Marasmius scorodonius in Escherichia coli the cDNA encoding the extracellular Msp2 peroxidase was cloned into the pBAD III expression plasmid. Expression of the protein with or without signal peptide was investigated in E. coli strains TOP10 and LMG194. Different PCR products were amplified for expression of the native target protein or a protein with a signal peptide. Omitting the native stop codon and adding six His-residues resulted in a fusion protein amenable to immune detection and purification by immobilised metal affinity chromatography. In E. coli the recombinant protein was produced in high yield as insoluble inclusion bodies. The influence of different parameters on MsP2 refolding was investigated. Active enzyme was obtained by glutathione-mediated oxidation in a medium containing urea, Ca²⁺, and hemin.     

Plasmid pGEX-5T: An alternative system for expression and purification of recombinant proteins

Summary A novel expression vector pGEX-5T was constructed which directs the synthesis of a fusion protein with a histidine-hexapeptide and glutathione-S-transferase at its N-terminus and the recombinant protein at its C-terminus inEscherichia coli. The designed fusion gene strategy allows the purification of soluble and insoluble recombinant proteins to homogeneity with single-step affinity chromatography using immobilized glutathione and metal chelating matrix, respectively. The principle and availability of this new expression system was respectively tested with the purification of a soluble and insoluble recombinant fusion protein containing 24 and 75 amino acids of the human thrombomodulin.     

Extracellular production and affinity purification of recombinant proteins with Escherichia coli using the versatility of the maltose binding protein

Recombinant proteins are essential products of today's industrial biotechnology. In this study we address two crucial factors in recombinant protein production: (i) product accessibility and (ii) product recovery. Escherichia coli, one of the most frequently used hosts for recombinant protein expression, does not inherently secrete proteins into the extracellular environment. The major drawback of this expression system is, therefore, to be found in the intracellular protein accumulation and hampered product accessibility. We have constructed a set of expression vectors in order to facilitate extracellular protein production and purification. The maltose binding protein from E. coli is used as fusion partner for several proteins of interest allowing an export to the bacteria's periplasm via both the Sec and the Tat pathway. Upon coexpression of a modified Cloacin DF13 bacteriocin release protein, the hybrid proteins are released into the culture medium. This essentially applies to a distinguished reporter molecule, the green fluorescent protein, for which an extracellular production was not reported so far. The sequestered proteins can be purified to approximate homogeneity by a simple, rapid and cheap procedure which utilizes the affinity of the maltose binding protein to α-1,4-glucans.     

Expression,purification and characterization of the interferon-inducible,antiviral and tumour-suppressor protein,human RNase L

The interferon (IFN)-inducible, 2′,5′-oligoadenylate (2-5A)-dependent ribonuclease L (RNase L) plays key role in antiviral defense of mammalian cells. Induction by IFN and activation by double-stranded RNA lead to 2-5A cofactor synthesis, which activates RNase L by causing its dimerization. Active RNase L degrades single-stranded viral as well as cellular RNAs causing apoptosis of virus-infected cells. Earlier, we had reported that expression of recombinant human RNase L caused RNA-degradation and cell-growth inhibition in E. coli without the need for exogenous 2-5A. Expression of human RNase L in E. coli usually leads to problems of leaky expression, low yield and degradation of the recombinant protein, which demands number of chromatographic steps for its subsequent purification thereby, compromising its biochemical activity. Here, we report a convenient protocol for expression of full-length, soluble and biochemically active recombinant human RNase L as GST-RNase L fusion protein from E. coli utilizing a single-step affinity purification with an appreciable yield of the highly purified protein. Recombinant RNase L was characterized by SDS-PAGE, immunoblotting and MALDI-TOF analysis. A semi-quantitative agarose-gel-based ribonuclease assay was developed for measuring its 2-5A-dependent RNase L activity against cellular large rRNAs as substrates. The optimized expression conditions minimized degradation of the protein, making it a convenient method for purification of RNase L, which can be utilized to study effects of various agents on the RNase L activity and its protein–protein interactions.     

Isotopically labeled expression in E. coli, purification, and refolding of the full ectodomain of the influenza virus membrane fusion protein

This paper describes methods to produce an isotopically labeled 23 kDa viral membrane protein with purified yield of 20 mg/L of Escherichia coli shake flask culture. This yield is sufficient for NMR structural studies and the protein production methods are simple, straightforward, and rapid and likely applicable to other recombinant membrane proteins expressed in E. coli. The target FHA2 protein is the full ectodomain construct of the influenza virus hemagglutinin protein which catalyzes fusion between the viral and the cellular endosomal membranes during infection. The high yield of FHA2 was achieved by: (1) initial growth in rich medium to A₆₀₀  8 followed by a switch to minimal medium and induction of protein expression; and (2) obtaining protein both from purification of the detergent-soluble lysate and from solubilization, purification, and refolding of inclusion bodies. The high cell density was achieved after optimization of pH, oxygenation, and carbon source and concentration, and the refolding protocol was optimized using circular dichroism spectroscopy. For a single residue of membrane-associated FHA2 that was obtained from purification and refolding of inclusion bodies, native conformation was verified by the ¹³CO chemical shifts measured using solid-state nuclear magnetic resonance spectroscopy.