Automated,High Productivity Purification and Analysis of Synthetic Peptides

Methods for peptide assembly consist of techniques that allow for construction of complex sequences. The advantage of solid-phase methodologies is automation of the repetitive processes of deprotecting, washing, and coupling protected amino acids (acylation). However, for difficult sequences the crude product contains a variety of side products that must be removed to provide the desired target peptide in sufficient concentration and purity. This paper illustrates that high efficiency purification method-development can be achieved by combining purification and analysis on a single platform. Incorporation of fast LC-based assays using polystyrene-based POROS® Perfusion Chromatography media permitted rapid overall processing times from crude peptide purification through fraction pooling and product verification. Application of these technologies to the purification of peptides at scales of 100 mg is demonstrated.     

An impurity characterization based approach for the rapid development of integrated downstream purification processes

In this study, we describe a new approach for the characterization of process‐related impurities along with an in silico tool to generate orthogonal, integrated downstream purification processes for biological products. A one‐time characterization of process‐related impurities from product expression in Pichia pastoris was first carried out using linear salt and pH gradients on a library of multimodal, salt‐tolerant, and hydrophobic charge induction chromatographic resins. The Reversed‐phase ultra‐performance liquid chromatography (UPLC) analysis of the fractions from these gradients was then used to generate large data sets of impurity profiles. A retention database of the biological product was also generated using the same linear salt and pH gradients on these resins, without fraction collection. The resulting two data sets were then analyzed using an in silico tool, which incorporated integrated manufacturing constraints to generate and rank potential three‐step purification sequences based on their predicted purification performance as well as whole‐process “orthogonality” for impurity removal. Highly ranked sequences were further examined to identify templates for process development. The efficacy of this approach was successfully demonstrated for the rapid development of robust integrated processes for human growth hormone and granulocyte‐colony stimulating factor.     

A combined screening and in silico strategy for the rapid design of integrated downstream processes for process and product-related impurity removal

Integrated designs of chromatographic processes for purification of biopharmaceuticals provides potential gains in operational efficiency and reductions of costs and material requirements. We describe a combined method using screening and in silico algorithms for ranking chromatographic steps to rapidly design orthogonally selective integrated processes for purifying protein therapeutics from both process- and product-related impurities. IFN-α2b produced in Pichia pastoris containing a significant product variant challenge was used as a case study. The product and product-related variants were screened on a set of 14 multimodal, ion exchange, and hydrophobic charge induction chromatography resins under various pH and salt linear gradient conditions. Data generated from reversed-phase chromatography of the fractions collected were used to generate a retention database for IFN-α2b and its variants. These data, in combination with a previously constructed process-related impurity database for P. pastoris, were input into an in silico process development tool that generated and ranked all possible integrated chromatographic sequences for their ability to remove both process and product-related impurities. Top-ranking outputs guided the experimental refinement of two successful three step purification processes, one comprising all bind-elute steps and the other having two bind-elute steps and a flowthrough operation. This approach suggests a new platform-like approach for rapidly designing purification processes for a range of proteins where separations of both process- and product-related impurities are needed.     

Single-step purification of a small non-mAb biologic by peptide-ELP-based affinity precipitation

Affinity precipitation using stimulus-responsive biopolymers such as elastin-like polypeptides (ELPs) have been successfully employed for the purification of monoclonal antibodies. In the current work, we extend these studies to the development of an ELP-peptide fusion for the affinity precipitation of the therapeutically relevant small non-mAb biologic, AdP. A 12-mer affinity peptide ligand (P10) was identified by a primary phage biopanning followed by a secondary in-solution fluorescence polarization screen. Peptide P10 and AdP interacted with a K_D of 19.5 µM. A fusion of P10 with ELP was then shown to be successful in selectively capturing the biologic from a crude mixture. While pH shifts alone were not sufficient for product elution, the use of pH in concert with fluid-phase modifiers such as NaCl, arginine, or ethylene glycol was effective. In particular, the use of pH 8.5 and an arginine concentration of 500 mM enabled >80% product recovery. The overall process performance evaluated by sodium dodecyl sulfate-polyacrylamide gel electrophoresis and reversed-phase ultra-performance liquid chromatography analyses indicated successful single-step purification of the biologic from an Escherichia coli lysate resulting in ∼90% purity and >80% recovery. These results demonstrate that phage display can be readily employed to identify a peptide ligand capable of successfully carrying out the purification of a non-antibody biological product using ELP-based affinity precipitation.     

Single‐step affinity purification of enzyme biotherapeutics: A platform methodology for accelerated process development

Downstream sample purification for quality attribute analysis is a significant bottleneck in process development for non‐antibody biologics. Multi‐step chromatography process train purifications are typically required prior to many critical analytical tests. This prerequisite leads to limited throughput, long lead times to obtain purified product, and significant resource requirements. In this work, immunoaffinity purification technology has been leveraged to achieve single‐step affinity purification of two different enzyme biotherapeutics (Fabrazyme® [agalsidase beta] and Enzyme 2) with polyclonal and monoclonal antibodies, respectively, as ligands. Target molecules were rapidly isolated from cell culture harvest in sufficient purity to enable analysis of critical quality attributes (CQAs). Most importantly, this is the first study that demonstrates the application of predictive analytics techniques to predict critical quality attributes of a commercial biologic. The data obtained using the affinity columns were used to generate appropriate models to predict quality attributes that would be obtained after traditional multi‐step purification trains. These models empower process development decision‐making with drug substance‐equivalent product quality information without generation of actual drug substance. Optimization was performed to ensure maximum target recovery and minimal target protein degradation. The methodologies developed for Fabrazyme were successfully reapplied for Enzyme 2, indicating platform opportunities. The impact of the technology is significant, including reductions in time and personnel requirements, rapid product purification, and substantially increased throughput. Applications are discussed, including upstream and downstream process development support to achieve the principles of Quality by Design (QbD) as well as integration with bioprocesses as a process analytical technology (PAT). © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:708–717, 2014     

Evidence that peptide deformylase and methionyl-tRNA(fMet) formyltransferase are encoded within the same operon in Escherichia coli.

Overexpression of the fms gene, the first translation unit of a dicistronic operon that also encodes methionyl-tRNA(fMet) formyltransferase in Escherichia coli, sustains the overproduction of peptide deformylase activity in crude extracts. This suggests that the fms gene encodes the peptide deformylase. Moreover, the fms gene product has a motif characteristic of metalloproteases, an activity compatible with deformylase. The corresponding protein could be purified to homogeneity. However, its enzymatic activity could not be retained during the purification procedure. As could be expected from the occurrence in its amino acid sequence of a zinc-binding motif characteristic of metallopeptidases, the purified fms product displayed one tightly bound zinc atom.     

Recombinant protein purification using complementary peptides as affinity tags

Affinity tags have become highly popular tools for purifying recombinant proteins from crude extracts by affinity chromatography. Besides, short peptides are excellent ligands for affinity chromatography, as they are not likely to cause an immune response in case of leakage into the product, they are more stable than antibodies to elution and cleaning conditions and they usually have very acceptable selectivity. Hydropathically complementary peptides designed de novo show enough selectivity to be used successfully as peptide ligands for protein purification from crude extracts. Recognition specificity and selectivity in the interaction between the complementary peptide pair His-Leu-Leu-Phe-Pro-Ile-Ile-Ile-Ala-Ala-Ser-Leu and Lys-Asn-Tyr-Pro-Lys-Lys-Lys-Met-Glu-Lys-Arg-Phe have been demonstrated by other authors. In this work, we designed a recombinant protein purification method using a peptide affinity tag that binds to a peptide-binding partner immobilized on a chromatographic matrix. The enhanced green fluorescent protein expressed (EGFP) in Escherichia coli was used as the model. The peptide Gly-Gly-Gly-His-Leu-Leu-Phe-Pro-Ile-Ile-Ile-Ala-Ala-Ser-Leu was synthesized by solid phase using the Fmoc chemistry and immobilized in NHS-Sepharose (PC-Sepharose). Gly residues were added as a spacer arm at the N terminus. The EGFP was expressed either with the fusion tag Lys-Asn-Tyr-Pro-Lys-Lys-Lys-Met-Glu-Lys-Arg-Phe on the C terminus (EGFP-CPTag) or without any fusion tag. After cell disruption, the extract was directly applied to the PC-Sepharose column equilibrated with 20mM sodium phosphate buffer, pH 7.0. The adsorbed EGFP-CPTag was then eluted with 1M Tris. The yield was 98% and the purification factor 4.6. By contrast, EGFP without tag pass through without interacting with the PC-Sepharose column. The method designed can be applied for the purification of other recombinant proteins.     

Analytical isotachophoresis in the analysis of synthetic peptides.

Two peptides, one undecapeptide and one decapeptide, have been synthesized by the solid phase method. Isotachophoresis has been used as an analytical tool to guide the purification of the peptides. This technique gives qualitative as well as quantitative information about the purification progress. Furthermore, the purity and identity of the final product can be established. The method is rapid, reproducible and easy to perform. Since isotachophoresis also can be used for amino acid analysis, it might have a wide use in peptide chemistry.The two peptides, having the primary sequences around the cross-linking site of fibrin, have been tested in vitro as inhibitors of the fibrin cross-linking. Both peptides were essentially inactive.     

MINLP models for the synthesis of optimal peptide tags and downstream protein processing

The development of systematic methods for the synthesis of downstream protein processing operations has seen growing interest in recent years, as purification is often the most complex and costly stage in biochemical production plants. The objective of the work presented here is to develop mathematical models based on mixed integer optimization techniques, which integrate the selection of optimal peptide purification tags into an established framework for the synthesis of protein purification processes. Peptide tags are comparatively short sequences of amino acids fused onto the protein product, capable of reducing the required purification steps. The methodology is illustrated through its application on two example protein mixtures involving up to 13 contaminants and a set of 11 candidate chromatographic steps. The results are indicative of the benefits resulting by the appropriate use of peptide tags in purification processes and provide a guideline for both optimal tag design and downstream process synthesis.     

An optimized Boc synthesis of indolicidin

Indolicidin, an antimicrobial peptide from bovine neutrophils containing five tryptophan out of a total of 13 residues, has the highest molar proportion of tryptophan of any known peptide sequence and is thus considered a difficult synthetic target. Conventional Boc chemistry can be applied to the synthesis of indolicidin with an appropriate choice of scavenger mixtures, reaction times and temperatures at the crucial acidolytic cleavage and deprotection step. In particular, treatment with HF/p-cresol/p-thiocresol (90:7:3) for 40 min at –8 °C results in a crude product containing ca. 90% indolicidin, from which the target compound can be isolated in satisfactory yields and purity after reverse-phase purification. The main byproducts arising during the synthesis and cleavage steps have been identified by HPLC with on-line electrospray mass spectrometric detection.     

Optimization of protein fusion partner length for maximizing in vitro translation of peptides

Using protein fusion partners for in vitro translation may increase solubility, assist in purification, or allow detection of small proteins and peptides. Here we show that the molar yield of peptide in a batch reaction may be maximized by optimizing the length of the translated product, which is composed of the fusion partner plus the peptide. Using truncated versions of GFP as a series of fusion partners, the molar yield increased approximately 3-fold as the length of the translated product was reduced from 250 to 100 amino acids. When the translated product was shortened below roughly 100 amino acids, molar yield fell as a result of proteolysis. This trend was verified using two fusion partners with different amino acid sequences. Furthermore, protease inhibitors were used to confirm that proteases were responsible for limiting accumulation of peptides below the optimal length.     

An optimized Boc synthesis of indolicidin

Summary Indolicidin, an antimicrobial peptide from bovine neutrophils containing five tryptophan out of a total of 13 residues, has the highest molar proportion of tryptophan of any known peptide sequence and is thus considered a difficult synthetic target. Conventional Boc chemistry can be applied to the synthesis of indolicidin with an appropriate choice of scavenger mixtures, reaction times and temperatures at the crucial acidolytic cleavage and deprotection step. In particular, treatment with HF/p-cresol/p-thiocresol (90:7:3) for 40 min at −8°C results in a crude product containing ca. 90% indolicidin, from which the target compound can be isolated in satisfactory yields and purity after reverse-phase purification. The main byproducts arising during the synthesis and cleavage steps have been identified by HPLC with on-line electrospray mass spectrometric detection.     

Exploratory synthesis of peptide-alpha-thioester segments spanning the polypeptide sequence of the delta-opioid receptor, a G protein-coupled receptor

We have decided to use the delta-opioid receptor (372 residues) as a model system to develop methods for the total chemical synthesis of G protein-coupled receptors. The most important feature of this receptor from a chemical synthesis perspective is the wealth of cysteines spread throughout its sequence, which are required for native chemical ligation. A total of 13 cysteines are located in the the delta-opioid receptor polypetide chain in both loop and putative transmembrane (TM) regions. We envisioned a synthesis of the polypeptide that would make use of peptide-alpha-thioesters ranging from 37 to 63 residues in length. Here, we report data from an exploratory synthesis of such a set of peptide-alpha-thioesters. For all seven peptides, the crude material approximately 30 residues into the synthesis was sufficiently homogeneous to make isolation and purification straightforward. Extension of the peptides to between 40 and 50 residues in length generally produced a significant decrease in the quality of the crude products, although in most cases, we judged that high purity peptides could probably be isolated. By 60 residues, however, the crude peptide product mixtures are probably too heterogeneous to purify to homogeneity by reversed-phase HPLC. In general, delta-opioid receptor peptides with a single predicted TM domain were sufficiently soluble to handle postcleavage and to analyze by reversed-phase HPLC, whereas 1.5 TM domains rendered the peptides too hydrophobic to handle or analyze by standard protocols. Given the challenges of chain assembly, handling, and purification of these peptides, a synthetic strategy that uses approximately 12 or 13 shorter peptide segments of 20-40 residues each is probably a more feasible approach.     

The Choice of HLA‐Associated Peptide Enrichment and Purification Strategy Affects Peptide Yields and Creates a Bias in Detected Sequence Repertoire

Understanding the most appropriate workflow for biochemical human leukocyte antigen (HLA)‐associated peptide enrichment prior to ligand sequencing is essential to achieve optimal sensitivity in immunopeptidomics experiments. The use of different detergents for HLA solubilization as well as complementary workflows to separate HLA‐bound peptides from HLA protein complex components after their immunoprecipitation including HPLC, C18 cartridge, and 5 kDa filter are described. It is observed that all solubilization approaches tested led to similar peptide ligand identification rates; however, a higher number of peptides are identified in samples lysed with CHAPS compared with other methods. The HPLC method is superior in terms of HLA‐I peptide recovery compared with 5 kDa filter and C18 cartridge peptide purification methods. Most importantly, it is observed that both the choice of detergent and peptide purification strategy creates a significant bias for the identified peptide sequences, and that allele‐specific peptide repertoires are affected depending on the workflow of choice. The results highlight the importance of employing a suitable strategy for HLA peptide enrichment and that the obtained peptide repertoires do not necessarily reflect the true distributions of peptide sequences in the sample.     

Preparation of Purified Polysaccharides from Rhizobium

A method is described for the preparation of purified polysaccharides from strains of Rhizobium in quantities large enough so that with an exhaustive purification scheme enough product is recovered for various characterization purposes. When steps in the purification process are eliminated, much larger amounts of crude gum are obtained.

Organisms were grown in liquid medium and the crude gum was precipitated along with the bacterial cells by a quaternary ammonium complexing agent. This precipitate was dissolved in salt solution, reprecipitated with ethanol or ethanol-acetone mixtures several times, followed by pressure filtration with membrane filters.

The same procedure should be applicable to commercial scale production in large fermentors if a use for the gum could be shown. The method also should be suitable for other organisms with similar growth habits.

     

Recombinant peptide fusion construction for protein-templated catalytic palladium nanoparticles

Although peptide-enabled synthesis of nanostructures has garnered considerable interest for use in catalytic applications, it has so far been achieved mostly via Fmoc based solid phase peptide synthesis. Consequently, the potential of longer peptides in nanoparticle synthesis have not been explored largely due to the complexities and economic constraints of this chemical synthesis route. This study examines the potential of a 45-amino acid long peptide expressed as fusion to green fluorescence protein (GFPuv) in Escherichia coli for use in palladium nanoparticle synthesis. Fed-batch fermentation with E. coli harboring an arabinose-inducible plasmid produced a product containing three copies of Pd4 peptide fused to N-terminus of GFPuv ((Pd4)₃-GFPuv). Using the intrinsic fluorescence of GFPuv, expression and enrichment of the fusion product was easily monitored. Crude lysate, desalted lysate, and an ion-exchange enriched fraction containing (Pd4)₃-GFPuv were used to test the hypothesis that high purity of the biologic material used as the nanoparticle synthesis template may not be necessary. Nanoparticles were characterized using a variety of material science techniques and used to catalyze a model Suzuki–Miyaura coupling reaction. Results demonstrated that palladium nanoparticles can be synthesized using the soluble cell extract containing (Pd4)₃-GFPuv without extensive purification or cleavage steps, and as a catalyst the crude mixture is functional.     

A simple and inexpensive sample-handling method for the semi-preparative RP-HPLC of polypeptides and non-polar peptide derivatives: pre-adsorption of samples

A simple method is described for the application onto HPLC columns of very crude or alternatively poorly soluble polypeptide samples prior to their chromatographic purification. The procedure involves the batch pre-adsorption of the crude polypeptide mixture from a dilute solution onto an appropriate preparative-grade chromatographic adsorbent, removal of the solvent by rotary evaporation or lyophilisation and then dry-packing the pre-adsorbed chromatographic material into guard column cartridges of suitable dimensions. The polypeptide products can then be eluted either by isocratic or gradient elution methods through the cartridge coupled in tandem with prepacked semi-preparative HPLC columns. This method has been successfully utilised for the routine RP-HPLC purification of polar and hydrophobic polypeptides prepared by solid phase peptide synthesis (SPPS) methods as well as peptide derivatives and intermediates used as part of SPPS procedures.     

Chemical synthesis, characterization and activity of RK-1, a novel alpha-defensin-related peptide.

The 32-residue peptide, RK-1, a novel kidney-derived three disulfide-bonded member of the antimicrobial alpha-defensin family, was synthesized by the continuous flow Fmoc-solid phase method. The crude, cleaved and S-reduced linear peptide was both efficiently folded and oxidized in an acidic solution of aqueous dimethyl sulfoxide. Following purification of the resulting product, it was shown by a variety of analytical techniques, including matrix assisted laser desorption time of flight mass spectrometry, to possess a very high degree of purity. The disulfide bond pairing of the synthetic peptide was determined by 1H-NMR spectroscopy and confirmed to be a Cys1-Cys6, Cys2-Cys4, Cys3-Cys5 arrangement similar to other mammalian alpha-defensin peptides. The synthetic RK-1 was also shown to inhibit the growth of Escherichia coli type strain NCTC 10418.     

Caprylic acid precipitation method for impurity reduction: An alternative to conventional chromatography for monoclonal antibody purification

We report the use of caprylic acid based impurity precipitation as (1) an alternative method to polishing chromatography techniques commonly used for monoclonal antibody purification and (2) an impurity reduction step prior to harvesting the bioreactor. This impurity reduction method was tested with protein A purified antibodies and with cell culture fluid. First, the operational parameters influencing precipitation of host cell proteins and high molecular weight aggregate in protein A pools were investigated. When used as a polishing step, the primary factor affecting purification and yield was determined to be pH. Caprylic acid precipitation was comparable to polishing IEX chromatography in reducing host cell protein and aggregate levels. A virus reduction study showed complete clearance of a model retrovirus during caprylic acid precipitation of protein A purified antibody. Caprylic acid mediated impurity precipitation in cell culture showed that the impurity clearance was generally insensitive to pH and caprylic acid concentration whereas yield was a function of caprylic acid concentration. Protein A purification of caprylic acid precipitated cell culture fluid generated less turbid product pool with reduced levels of host cell proteins and high molecular weight aggregate. The results of this study show caprylic acid precipitation to be an effective purification method that can be incorporated into a production facility with minimal cost as it utilizes existing tanks and process flow. Eliminating flow through chromatography polishing step can provide process intensification by avoiding the process tank volume constraints for high titer processes. Biotechnol. Bioeng. 2012; 109: 2589–2598. © 2012 Wiley Periodicals, Inc.