Recombinant Elastin-Based Bioelastomers for Biomedical Applications

Recombinant elastin-based proteins (ELPs) are used in applications that include therapeutics, drug delivery, and tissue engineering due to their biocompatibility and unique ability to undergo simple coacervation. Here, we describe a cost-effective method to purify ELPs utilizing salt precipitation and their reversible phase transition property when heated above their lower critical solution temperature (LCST). Furthermore, we describe the post-translational modification of converting tyrosine residues to L-3,4-dihydroxyphenylalanine (DOPA) for adhesive applications.

Protein Extraction and Purification by Differential Solubilization

The preparation of purified soluble proteins for biochemical studies is essential and the solubility of a protein of interest in various media is central to this process. Selectively altering the solubility of a protein is a rapid and economical step in protein purification and is based on exploiting the inherent physicochemical properties of a polypeptide. Precipitation of proteins, released from cells upon lysis, is often used to concentrate a protein of interest before further purification steps (e.g., ion exchange chromatography, size exclusion chromatography etc).Recombinant proteins may be expressed in host cells as insoluble inclusion bodies due to various influences during overexpression. Such inclusion bodies can often be solubilized to be reconstituted as functional, correctly folded proteins.In this chapter, we examine strategies for extraction/precipitation/solubilization of proteins for protein purification. We also present bioinformatic tools to aid in understanding a protein's propensity to aggregate/solubilize that will be a useful starting point for the development of protein extraction, precipitation, and selective re-solubilization procedures.

Simplified Enzymatic Synthesis of 2-Keto-3-Deoxy-D-Gluconate from D-Gluconate Using the Gluconate Dehydratase from Thermoproteus tenax

Many research areas, e.g., basic research but also applied fields of biotechnology, biomedicine, and diagnostics often suffer from the unavailability of metabolic compounds. This is mostly due to missing easy and efficient synthesis procedures. We herein describe the biocatalytic/enzymatic production of 2-keto-3-deoxy-D-gluconate, an intermediate of central metabolic pathways in all three domains of life and also of bacterial polysaccharides, lipopolysaccharides, and cell wall components. The method is based on the gluconate dehydratase from the hyperthermophilic crenarchaeon Thermoproteus tenax, which can be easily recombinantly overproduced in Escherichia coli and-due to its intrinsic thermostability-rapidly be purified by two precipitation steps. The enzyme completely converts D-gluconate to solely stereochemically pure KDG, taking benefits from the enol-keto-tautomerism of the primary reaction product. The final product can then easily be separated from the protein by ultrafiltration. The simple one-step procedure, which is suitable at least for the lab-scale/gram-scale production of KDG, replaces lengthy multi-step reactions and is easily scalable. This approach also illustrates the great application potential of Archaea with their unusual metabolic pathways and enzymes for the synthesis of added value products.

Isolation of Outer Membrane Vesicles from Helicobacter pylori

Outer membrane vesicles (OMV) shed by pathogenic bacteria have multifunctional roles in disease initiation and progression. Further, their efficacy as novel vaccines has underscored their importance as potential therapeutics. Consequently, to advance allied research related to their immunogenicity and pathogenicity it is important to separate these vesicular structures from parental cells and demonstrate them to be free from cellular debris and other non-vesicle-related constituents such as protein aggregates. To do so represents a key step in initiating OMV-related studies and the techniques and strategies adopted by the H. pylori community to achieve this will be the focus of this chapter.The key methods used typically to obtain a heterogeneous mixture of OMV (size range: ~20-300 nm in diameter) include growth of bacteria in broth culture followed by differential centrifugation, filtration, and concentration to separate OMV from the intact organisms. Additional measures may be adopted to further size-fractionate the population of OMV including gel filtration or density gradient ultra-centrifugation in order to facilitate differentiation between the activities of small versus large OMV, as recent studies have demonstrated differential modes of entry into host cells as well as size-dependent differences in the OMV proteome (Turner et al., Front Immunol 9:1466, 2018). The OMV from H. pylori harbor many of the virulence factors associated with gastric disease including the CagA oncoprotein, the cytotoxin VacA, and the HtrA protease (Olofsson et al., mBio 5:e00979-14, 2014; Mullaney et al., Proteomics Clin Appl 3:785-96, 2009) and their close association with areas of cell-cell contact and efficient endocytosis supports a role for these complexes in gastric disease (Turkina et al., FEMS Microbiol Lett 362:fnv076, 2015).

Abundant plasma protein depletion using ammonium sulfate precipitation and Protein A affinity chromatography

Plasma is a highly valuable resource for biomarker research since it is easy obtainable and contains a high amount of information on patient health status. Although advancements in the field of proteomics enabled analysis of the plasma proteome, identification of low abundant proteins remains challenging due to high complexity and large dynamic range. In order to reduce the dynamic range of protein concentrations, a tandem depletion technique consisting of ammonium sulfate precipitation and Protein A affinity chromatography was developed. Using this method, 50% of albumin, together with other high abundant proteins such as alpha-1-antitrypsin, was depleted from the plasma sample at 20% to 40% ammonium sulfate saturation levels. In combination with immunoglobulin removal using a Protein A column, this technique delivered up to 40 new low- to medium abundance protein identifications when performing a shotgun mass spectrometry analysis. Compared to non-depleted plasma, 270 additional protein spots were observed during 2D-PAGE analysis. These results illustrate that this tandem depletion method is equivalent to commercial kits which are based on immune-affinity chromatography. Moreover, this method using Protein A immunoglobulin depletion was shown to be highly reproducible and a minimal amount of non-target proteins was depleted. The combination of ammonium sulfate precipitation and Protein A affinity chromatography offers a low cost, efficient, straightforward and reproducible alternative to commercial kits, with proteins remaining in native conformation, allowing protein activity and protein interaction studies.

Production and Purification of Polyclonal Antibodies

Polyclonal antibodies consist of a mixture of antibodies produced by multiple B-cell clones that have differentiated into antibody-producing plasma cells in response to an immunogen. Polyclonal antibodies raised against an antigen recognize multiple epitopes on a target molecule, which results in a signal amplification in indirect immunoassays including immune-electron microscopy. In this chapter, we present a basic procedure to generate polyclonal antibodies in rabbits.

Optimization of tetanus toxoid ammonium sulfate precipitation process using response surface methodology

Tetanus toxoid (TTd) is a highly immunogenic, detoxified form of tetanus toxin, a causative agent of tetanus disease, produced by Clostridium tetani. Since tetanus disease cannot be eradicated but is easily prevented by vaccination, the need for the tetanus vaccine is permanent. The aim of this work was to investigate the possibility of optimizing TTd purification, i.e., ammonium sulfate precipitation process. The influence of the percentage of ammonium sulfate, starting amount of TTd, buffer type, pH, temperature, and starting purity of TTd on the purification process were investigated using optimal design for response surface models. Responses measured for evaluation of the ammonium sulfate precipitation process were TTd amount (Lf/mL) and total protein content. These two parameters were used to calculate purity (Lf/mgPN) and the yield of the process. Results indicate that citrate buffer, lower temperature, and lower starting amount of TTd result in higher purities of precipitates. Gel electrophoresis combined with matrix-assisted laser desorption ionization-mass spectrometric analysis of precipitates revealed that there are no inter-protein cross-links and that all contaminating proteins have pIs similar to TTd, so this is most probably the reason for the limited success of purification by precipitation.

Differential Precipitation and Solubilization of Proteins

Differential protein precipitation is a rapid and economical step in protein purification and is based on exploiting the inherent physicochemical properties of the polypeptide. Precipitation of recombinant proteins, lysed from the host cell, is commonly used to concentrate the protein of choice before further polishing steps with more selective purification columns (e.g., His-Tag, Size Exclusion, etc.). Recombinant proteins can also precipitate naturally as inclusion bodies due to various influences during overexpression in the host cell. Although this phenomenon permits easier initial separation from native proteins, these inclusion bodies must carefully be differentially solubilized so as to reform functional, correctly folded proteins. Here, appropriate bioinformatics tools to aid in understanding a protein's propensity to aggregate and solubilize are explored as a backdrop for a typical protein extraction, precipitation, and selective resolubilization procedure, based on a recombinantly expressed protein.

A simple, rapid and cost-effective process for production of latex clearing protein to produce oligopolyisoprene molecules

Aiming at finding feasible alternatives for rubber waste disposal, the partial enzymatic degradation of poly(cis-1,4-isoprene)-containing materials represents a potential solution. The use of rubber-degrading enzymes and the biotransformation of rubber into new materials is limited by the high costs associated with the production and purification of the enzyme and the complexity of the process. This study presents a simple and low-cost procedure to obtain purified latex clearing protein (Lcp), an enzyme capable of cleaving the double bonds of poly(cis-1,4-isoprene) in presence of oxygen to produce different size of oligomers with terminal aldehyde and ketone groups, respectively. The gene coding for Lcp1_VH2 from Gordonia polyisoprenivorans strain VH2 was overexpressed in Escherichia coli C41 (DE3), and by using an auto-induction medium high protein yields were obtained. The cultivation process was described and compared with an IPTG-inducible medium previously used. Purification of the enzyme was performed using salting out precipitation with ammonium sulfate. Different salt concentrations and pH were tested in order to find the optimal for purification, obtaining a concentration of 60mg Lcp per l. The enzymatic activity of the purified enzyme was measured by an oxygen consumption assay in the presence of polyisoprene latex. Volumetric activities of 0.16Uml^-1 were obtained at optimal conditions of temperature and pH. The results showed an active and partial purified fraction of Lcp1_VH2, able to cleave the backbone of poly(cis-1,4-isoprene) and to produce degradation products that were identified with staining methodologies (Schiff reagent for aldehyde groups and 2,4-DNPH for carbonyl groups) and characterized using nuclear magnetic resonance (NMR). Thirteen different storage conditions were tested for the purified enzyme analyzing the enzymatic activity after 1 and 3 months. Lcp1_VH2, as an ammonium sulfate precipitate, was stable, easy to handle and sufficiently active for further analysis. The described methodology offers the possibility to upscale the process and to produce large amounts of this protein.