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.     

High‐throughput ion exchange purification of positively charged recombinant protein in the presence of negatively charged dextran sulfate

Product quality analyses are critical for developing cell line and bioprocess producing therapeutic proteins with desired critical product quality attributes. To facilitate these analyses, a high‐throughput small‐scale protein purification (SSP) is required to quickly purify many samples in parallel. Here we develop an SSP using ion exchange resins to purify a positively charged recombinant growth factor P1 in the presence of negatively charged dextran sulfate supplemented to improve the cell culture performance. The major challenge in this work is that the strong ionic interaction between P1 and dextran sulfate disrupts interaction between P1 and chromatography resins. To solve this problem, we develop a two‐step SSP using Q Sepharose Fast Flow (QFF) and SP Sepharose XL (SPXL) resins to purify P1. The overall yield of this two‐step SSP is 78%. Moreover, the SSP does not affect the critical product quality attributes. The SSP was critical for developing the cell line and process producing P1. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:516–520, 2014     

Single-column purification of recombinant human neurotrophin-3 (hNT3) by using the intein mediated self-cleaving system

The gene of human neurotrophin-3 (hNT3), a 380 bp fragment corresponding to a 14 kDa protein, was amplified by PCR with genome DNA of human whole blood as the template and cloned into a vector pTXB1. The recombinant including the hNT3 gene was expressed in E. coli and the target product was in the form of inclusion bodies. After denaturation and renaturation, the hNT3 was purified on an affinity column by a self-cleaving intein. The bioactivity assay showed that the purified hNT3 induced profuse neurite outgrowth from the dorsal root ganglia (DRG) explants.     

High-throughput process development for recombinant protein purification

Methods development in chromatographic purification processes is a complex operation and has traditionally relied on trial and error approaches. The availability of a large number of commercial media, choice of different modes of chromatography, and diverse operating conditions contribute to the challenging task of accelerating methods development. In this paper, we describe a novel microtiter-plate based screening method to identify the appropriate sequence of chromatographic steps that result in high purities of bioproducts from their respective culture broths. Protein mixtures containing the bioproduct were loaded on aliquots of different chromatographic media in microtiter plates. Serial step elution of the proteins, in concert with bioproduct-specific assays, resulted in the identification of "active fractions" containing the bioproduct. The identification of a successful chromatographic step was based on the purity of the active fractions, which were then pooled and used as starting material for screening the next chromatographic dimension. This procedure was repeated across subsequent dimensions until single band purities of the protein were obtained. The sequence of chromatographic steps and the corresponding operating conditions identified from the screen were validated under scaled-up conditions. Various modes of chromatography including hydrophobic interaction, ion exchange (cation and anion exchange) and hydrophobic charge-induction chromatography (HCIC), and different operating conditions (pH, salt concentration and type, etc.) were employed in the screen. This approach was employed to determine the sequence of chromatographic steps for the purification of recombinant alpha-amylase from its cell-free culture broth. Recommendations from the screen resulted in single-band purity of the protein under scaled-up conditions. Similar results were observed for an scFv-beta-lactamase fusion protein. The use of a miniaturized screen enables the parallel screening of a wide variety of actual bioprocess media and conditions and represents a novel paradigm approach for the high-throughput process development of recombinant proteins.     

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.     

Bispecific antibody process development: Assembly and purification of knob and hole bispecific antibodies

Production of knob and hole dual light chain bispecific antibodies poses several unique challenges for development of a feasible industrial scale manufacturing process. We developed an efficient process for the assembly and purification of knob and hole dual light chain bispecific antibodies. Two distinct half‐antibodies targeting two different antigens were expressed separately in Escherichia coli cells and captured independently using Protein A chromatography. When combined, the knob and hole mutations in the CH3 domains promoted heterodimer formation. The hinge region disulfides were reduced and reoxidized to form the disulfide bridge between the two complementary half antibodies. Unreacted half antibodies, noncovalently linked homodimers, covalently linked homodimers, and noncovalently linked heterodimers are impurities closely related to the product of interest and are challenging to remove by standard processes. Characterization of the molecular properties of the half antibodies and high‐throughput screening predicted column chromatography performance and allowed for rapid development of downstream purification steps for removal of unique product‐related and process‐related impurities. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:397–404, 2018     

Rapid automated detergent screening for the solubilization and purification of membrane proteins and complexes

Membrane proteins constitute about one third of proteins encoded by all genomes, but only a small percentage have their structures deposited in the Protein Data Bank. One bottleneck in the pipeline from expression to structure determination is the identification of detergents that maintain the protein in a soluble, stable, and active state. Here, we describe a small‐scale automated procedure to easily and rapidly screen detergents for the solubilization and purification of membrane proteins, to perform detergent exchange, or to identify conditions preserving protein interactions in complexes. Hundreds of conditions can be tested in a few hours to select detergents that keep proteins folded and nonaggregated, from single membrane preparations of cells overexpressing the protein(s) of interest. Thirty‐one prokaryotic, eukaryotic, and viral membrane proteins were analyzed by our small‐scale procedure to identify the best‐associated detergents. Examples of results obtained with a bitopic and multitopic membrane proteins and membrane protein complexes are presented in more detail. DDM, DM, DMNG, TritonX‐100, LAPAO, and Fos‐12 appeared effective for successful membrane solubilization and protein purification of most selected targets. Eukaryotic proteins are in general more difficult to extract and purify from Escherichia coli membranes than prokaryotic proteins. The protocol has been developed for His‐tagged proteins, but can readily be adapted to other affinity tags by adjusting the chromatography resin and the buffer composition.     

Novel and economical purification of recombinant proteins: intein-mediated protein purification using in vivo polyhydroxybutyrate (PHB) matrix association

This work combines two well-established technologies to generate a breakthrough in protein production and purification. The first is the production of polyhydroxybutyrate (PHB) granules in engineered strains of Escherichia coli. The second is a recently developed group of self-cleaving affinity tags based on protein splicing elements known as inteins. By combining these technologies with a PHB-specific binding protein, a self-contained protein expression and purification system has been developed. In this system, the PHB-binding protein effectively acts as an affinity tag for desired product proteins. The tagged product proteins are expressed in E. coli strains that also produce intracellular PHB granules, where they bind to the granules via the PHB-binding tag. The granules and attached proteins can then be easily recovered following cell lysis by simple mechanical means. Once purified, the product protein is self-cleaved from the granules and released into solution in a substantially purified form. This system has been successfully used at laboratory scale to purify several active test proteins at reasonable yield. By allowing the bacterial cells to effectively produce both the affinity resin and tagged target protein, the cost associated with the purification of recombinant proteins could be greatly reduced. It is expected that this combination of improved economics and simplicity will constitute a significant breakthrough in both large-scale production of purified proteins and enzymes and high-throughput proteomics studies of peptide libraries.     

A practical strategy for using miniature chromatography columns in a standardized high‐throughput workflow for purification development of monoclonal antibodies

The emergence of monoclonal antibody (mAb) therapies has created a need for faster and more efficient bioprocess development strategies in order to meet timeline and material demands. In this work, a high‐throughput process development (HTPD) strategy implementing several high‐throughput chromatography purification techniques is described. Namely, batch incubations are used to scout feasible operating conditions, miniature columns are then used to determine separation of impurities, and, finally, a limited number of lab scale columns are tested to confirm the conditions identified using high‐throughput techniques and to provide a path toward large scale processing. This multistep approach builds upon previous HTPD work by combining, in a unique sequential fashion, the flexibility and throughput of batch incubations with the increased separation characteristics for the packed bed format of miniature columns. Additionally, in order to assess the applicability of using miniature columns in this workflow, transport considerations were compared with traditional lab scale columns, and performances were mapped for the two techniques. The high‐throughput strategy was utilized to determine optimal operating conditions with two different types of resins for a difficult separation of a mAb monomer from aggregates. Other more detailed prediction models are cited, but the intent of this work was to use high‐throughput strategies as a general guide for scaling and assessing operating space rather than as a precise model to exactly predict performance. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:626–635, 2014     

Rapid extraction and purification of environmental DNA for molecular cloning applications and molecular diversity studies

A rapid method for the extraction and purification of DNA from environmental samples for molecular cloning applications was developed. The indigenous cells from plant debris, organic materials, sediments, and soils were lysed directly by using DAS-I^Z solution and the nucleic acids were precipitated with isopropanol. A simple purification step using DAS-II^Z solution without binding matrix produced highly pure, colorless and undegraded DNA with molecular weight of more than 20 kb. The superiority of this method was tested for wide applications in molecular cloning, i.e., construction of genomic library by using Lambda DASH^(R)II Vector and Gigapack^(R)III XL, plasmid library, cloning of gene encoding protease, and molecular microbial diversity analysis. An additional advantage of this method is that only 0.1 g of sample is required, if analysis of many samples in short time should be done. To extract large amounts of environmental DNA for molecular cloning lasts only 30 min and to purify it less than 1 h.     

Utilization of protein splicing for purification of the human growth hormone

Developing simple and reliable methods to purify recombinant proteins is among the most important problems of modern biotechnology. It is of particular interest to take advantage of protein splicing for this purpose. Affinity tagging of inteins allows the use of regular protocols for protein purification. Autocatalytic excision of the tagged intein yields the pure protein lacking N-terminal formylmethionine. A new purification technique was developed on the basis of protein splicing for the human growth hormone. The Mxe GyrA intein with the histidine tag or cellulose-binding domain was used as a self-removable affinity unit. The resulting two-step purification protocol makes it possible to obtain the human growth hormone having the native N terminus with minimal losses.     

Engineering a recyclable elastin‐like polypeptide capturing scaffold for non‐chromatographic protein purification

Previously, we reported a non‐chromatographic protein purification method exploiting the highly specific interaction between the dockerin and cohesin domains from Clostridium thermocellum and the reversible aggregation property of elastin‐like polypeptide (ELP) to provide fast and cost‐effective protein purification. However, the bound dockerin‐intein tag cannot be completely dissociated from the ELP‐cohesin capturing scaffold due to the high binding affinity, resulting in a single‐use approach. In order to further reduce the purification cost by recycling the ELP capturing scaffold, a truncated dockerin domain with the calcium‐coordinating function partially impaired was employed. We demonstrated that the truncated dockerin domain was sufficient to function as an effective affinity tag, and the target protein was purified directly from cell extracts in a single binding step followed by intein cleavage. The efficient EDTA‐mediated dissociation of the bound dockerin‐intein tag from the ELP‐cohesin capturing scaffold was realized, and the regenerated ELP capturing scaffold was reused in another purification cycle without any decrease in the purification efficiency. This recyclable non‐chromatographic based affinity method provides an attractive approach for efficient and cost‐effective protein purification. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29:968–971, 2013     

His tag effect on solubility of human proteins produced in Escherichia coli: a comparison between four expression vectors

We have compared four different vectors for expression of proteins with N- or C-terminal hexahistidine (His6) tags in Escherichia coli by testing these on 20 human proteins. We looked at a total recombinant protein production levels per gram dry cell weight, solubility of the target proteins, and yield of soluble and total protein when purified by immobilized metal ion affinity purification. It was found that, in general, both N- and C-terminal His6 tags have a noticeable negative affect on protein solubility, but the effect is target protein specific. A solubilizing fusion tag was able to partly counteract this negative effect. Most target proteins could be purified under denaturing conditions and about half of the proteins could be purified under physiological conditions. The highest protein production levels and yield of purified protein were obtained from a construct with C-terminal His tag. We also observe a large variation in cell growth rate, which we determined to be partly caused by the expression vectors and partly by the targets. This variation was found to be independent of the production level, solubility and tertiary structure content of the target proteins.     

High‐throughput mAb expression and purification platform based on transient CHO

A high‐cell‐density transient transfection system was recently developed in our laboratory based on a CHO‐GS‐KO cell line. This method yields monoclonal antibody titers up to 350 mg/L from a simple 7‐day process, in volumes ranging from 2 mL to 2 L. By performing transfections in 24‐deep‐well plates, a large number of mAbs can be expressed simultaneously. We coupled this new high‐throughput transfection process to a semiautomated protein A purification process. Using a Biomek FX^p liquid handling robot, up to 72 unique mAbs can be simultaneously purified. Our primary goal was to obtain >0.25 mg of purified mAb at a concentration of >0.5 mg/mL, without any concentration or buffer‐exchange steps. We optimized both the batch‐binding and the batch elution steps. The length of the batch‐binding step was important to minimize mAb losses in the flowthrough fraction. The elution step proved to be challenging to simultaneously maximize protein recovery and protein concentration. We designed a variable volume elution strategy based on the average supernatant titer. Finally, we present two case studies. In the first study, we produced 56 affinity maturation mAb variants at an average yield of 0.33 ± 0.05 mg (average concentration of 0.65 ± 0.10 mg/mL). In a second study, we produced 42 unique mAbs, from an early‐stage discovery effort, at an average yield of 0.79 ± 0.31 mg (average concentration of 1.59 ± 0.63 mg/mL). The combination of parallel high‐yielding transient transfection and semiautomated high‐throughput protein A purification represents a valuable mAb drug discovery tool. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:239–247, 2015     

Peptides from the SARS-associated coronavirus as tags for protein expression and purification

Protein tagging with a peptide is a commonly used technique to facilitate protein detection and to carry out protein purification. Flexibility with respect to the peptide tag is essential since no single tag suites all purposes. This report describes the usage of two short peptides from the SARS-associated coronavirus nucleocapsid (SARS-N) protein as protein tags. Plasmids for the generation of tagged proteins were generated by ligating synthetic oligonucleotides for the peptide-coding regions downstream of the protein coding sequence. The data show recognition of prokaryotically expressed HIV-1 Gag/p24 fusion protein by Western blot and efficient affinity purification using monoclonal antibodies against the tags. The SARS peptide antibody system described presents an alternative tagging opportunity in the growing field of protein science.     

Rapid purification and crystal structure analysis of a small protein carrying two terminal affinity tags

Small peptide tags are often fused to proteins to allow their affinity purification in high-throughput structure analysis schemes. To assess the compatibility of small peptide tags with protein crystallization and to examine if the tags alter the three-dimensional structure, the N-terminus of the chicken alpha-spectrin SH3 domain was labeled with a His6 tag and the C-terminus with a StrepII tag. The resulting protein, His6-SH3-StrepII, consists of 83 amino-acid residues, 23 of which originate from the tags. His6-SH3-StrepII is readily purified by dual affinity chromatography, has very similar biophysical characteristics as the untagged protein domain and crystallizes readily from a number of sparse-matrix screen conditions. The crystal structure analysis at 2.3 A resolution proves native-like structure of His6-SH3-StrepII and shows the entire His6 tag and part of the StrepII tag to be disordered in the crystal. Obviously, the fused affinity tags did not interfere with crystallization and structure analysis and did not change the protein structure. From the extreme case of His6-SH3-StrepII, where affinity tags represent 27% of the total fusion protein mass, we extrapolate that protein constructs with N- and C-terminal peptide tags may lend themselves to biophysical and structural investigations in high-throughput regimes.     

Rapid screening and scale-up of ultracentrifugation-free,membrane-based procedures for purification of His-tagged membrane proteins

This study develops procedures to rapidly screen conditions for purification of membrane proteins (MPs) using 96-well plates containing nickel-functionalized membranes. In addition to their application in the pharmaceutical industry, MPs are important components of new sensors, synthetic membranes, and bioelectronic devices. However, purification of MPs is challenging due to their hydrophobic exterior, which requires stabilization in amphipathic detergent micelles. We examined the extent of extraction of the light-driven sodium transporter, Krokinobacter eikastus rhodopsin 2 (KR2) heterologously expressed in Escherichia coli using different salts and maltoside-based detergents. The extraction was followed by subsequent affinity purification in membranes functionalized with Ni²⁺-nitrilotriacetate complexes that bind the His-tagged KR2. We also employed a hydrophobic chelator to separate detergent micelles from the aqueous phase as an initial isolation step prior to affinity purification. Unlike conventional resin-based capture, which can take a full day or more, the membrane-based screening of purification conditions takes only a few hours, and its scale-up involves changing from a 96-well format to a larger membrane module. The novelty of the method lies in utilizing membrane-based ultracentrifugation-free purification of MPs from cell membrane fragments; the optimized purification conditions from the screening method can potentially be applied to large-scale/conventional resin-based purification of MPs.