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Recombinant protein expression and purification is a powerful tool to synthesize biomaterials with high reproducibility. Owing largely to the advent of commercialized molecular cloning, custom recombinant plasmids can be purchased from several suppliers, which significantly reduces the time to work with materials like ELPs. Similarly, plasmids can be requested directly from the originating lab when the original work was supported by a federal contract and the future work will be for non-profit use. The full ELP amino acid sequence has been previously published for several ELP variants31. However, the process from expression to eventual purification of recombinant proteins involves a number of critical steps that can commonly lead to reduced yields or a lower quality product. Some of the most common issues for ELP preparation arise in one of the following: (1) quality of stored bacterial stocks, (2) the first freeze-thaw cycle to disrupt the bacterial membrane, and (3) protein purification through thermal cycling.
A major difference between protein expression and other non-biological means of producing materials is that we are leveraging the biological machinery of recombinant hosts to synthesize the polymers. Subsequently, this technique comes with a unique limitation: cellular death or damage. Cell death most commonly manifests itself as a reduced number of bacterial colonies after streaking a plate or abnormally small colonies that grow relatively slowly. Bacterial stocks, if maintained carefully, can remain stable for years; however, successive freeze-thaw cycles due to repeated use or freezer failure can reduce cell viability or lead to DNA damage. Typical BL21 bacteria stocks use between 10% and 40% glycerol by volume mixed with suspended cells. The purpose of the glycerol is to reduce membrane damage from nucleating ice crystals during freezing. Therefore, using low concentrations (<10%) can lead to a compromised membrane, while higher concentrations (>40%) can suppress the freezing point sufficiently to where the stock never freezes leading to cell death. However, even within optimal glycerol levels, bacterial stocks should not be allowed to fully thaw as a combination of membrane damage from re-freezing and cytotoxic effects from the glycerol can lead to reduced stock viability and DNA damage. Therefore, if it is observed that a bacterial stock results in a low colony count or that the cells are dividing at a consistently slow rate (manifested as a slow OD600 ramp rate during expression), re-transforming the plasmid and making a new stock is a simple first approach to troubleshoot this problem. With this in mind, to ensure the long-term upkeep of bacterial stocks and integrity of DNA, it is best to store the copies of your plasmid as purified DNA frozen in water and not within cells. Storing DNA in this way will ensure that in unforeseen events such as a failed stock or freezer failure, a reliable source of the original DNA can be used for transformation.
Another critical step in ELP fabrication is the purification of the target protein from the expression host. Protein extraction from E. coli is achieved by breaking the cell wall using nucleating ice crystals that form throughout the suspended cell lysate upon freezing, which is further compounded with successive freeze-thaw cycles. Alternative methods for rupturing the cell wall can be utilized such as sonication or a press. In particular, consecutive freeze-thawing of the lysate is advantageous as it only requires a freezer and no other specialty equipment. However, this procedure nonspecifically releases DNA, RNA, and protein contaminants, in addition to proteases that have the potential to degrade the target protein. Therefore, to avoid contamination and reduced yield, deoxyribonuclease I (DNase) and phenylmethanesulfonyl fluoride (PMSF) are added to the cell lysate to degrade the DNA and inhibit proteases, respectively. The presence of DNA prior to the addition of DNase can be observed visually as a 'stringy' appearance throughout the re-suspended cell lysate following the first thaw. DNase actively degrades this DNA and thus reduces the viscosity of the cell lysate making it easier to purify via centrifugation. Optimal break down of DNA can be visually confirmed by ensuring that the cell lysate appears to be entirely liquid and that the stringy appearance is no longer visible. We have observed in practice that the addition of ~0.1 mg of DNase per mL cell lysate is sufficient to achieve necessary degradation. However, if the presence of DNA is still observed, more DNase can be added followed by an additional two to three hours of agitation. A similar issue can also arise if DNase is added prematurely before any of the lysate has had the potential to sufficiently thaw. In this case, the colder temperatures can limit the efficiency of DNA degradation due to the premature inactivation of DNase. To avoid this issue, it is often best practice to allow the re-suspended pellet to thaw for approximately 8 hours prior to treatment with DNase. In addition, if low protein yields are reported and the breakdown of DNA has been sufficient, the addition of more PMSF to help further reduce potential protein degradation from proteases may be required.
Additional considerations for ensuring optimal expression of ELPs include a careful understanding of the benefits and limitations of a chosen antibiotic. Here, pET15b vectors containing an ampicillin resistance gene were used for protein expression. Functionally, the pET vector series allow for significant protein expression with as much as 50% of a bacterium's protein expression dedicated to the target protein following a successful induction32,33. However, ampicillin as a selection antibiotic comes with some limitations that may interfere with optimum expression. First, degradation of ampicillin in the presence of E. coli can occur rapidly due to the release of beta-lactamase. If a sufficient quantity of the ampicillin is degraded, the ampicillin-encoding plasmid (i.e. the ELP-encoding plasmid) may be lost entirely. As a result, when expressing ELPs for longer durations, protein expression levels should be carefully monitored at successive time points to ensure sufficient amount of the ELP-encoding gene remains to allow for desirable expression. Possible methods for troubleshooting the buildup of beta-lactamases include spinning down the starter culture and re-suspending the cells in antibiotic-free medium prior to inoculating the expression medium. This process effectively limits the transfer of antibiotic-degrading enzymes and ensures a greater portion of the cells contain the target-protein-encoding vector. Additionally, ampicillin has a limited shelf life of approximately two to three weeks. Therefore, culture plates for protein expression should be stored at 4 °C for a maximum of two weeks prior to use. Finally, to ensure the efficacy of ampicillin within the starter and expression media, the ampicillin stock solution should be produced fresh immediately before use, as long-term storage may lead to a less effective antibiotic.
The presence of an LCST allows for the simple purification of ELPs through thermal cycling. Specifically, at a higher temperature and in the presence of salts, entropic forces cause ELPs to become less soluble and subsequently form a polymer-rich coacervate phase. On the other hand, at lower temperatures, ELPs remain soluble and readily dissolve into the solution. Cycling between these two temperature regimes coupled with centrifugation steps to collect and discard the non-ELP-containing phase successively concentrates the protein and simultaneously reduces the existence of non-ELP contaminants.
However, there are a number of stages where ELPs can be lost in this purification process. First, prior to every cold spin, the protein-containing solution is alkalized to a pH of 9.0. This higher pH serves to deprotonate certain amino acids on the protein backbone, effectively leaving them in a charged state and further enhancing their solubility. Consequently, foregoing this step or not allowing sufficient time for protein dissolution can lead to a reduction in yield as non-solubilized proteins will be pelleted during centrifugation and discarded.
Similarly, target proteins can be lost during the hot spin procedure when the ELP is pelleted. Initially, NaCl is added to the protein-rich supernatant to reduce the solubility of the ELP. The salts work to shield electrostatic interactions between the protein and water molecules, causing the protein to separate from the aqueous phase. This effect is amplified by heating the solution, which, due to entropic effects, further breaks down the hydrous 'cage' surrounding ELPs and forces the aggregation of the proteins. At lower protein concentrations (i.e., the first thermal cycle), the addition of salts alone is often insufficient to cause this phase separation. However, as the concentration of protein increases (i.e., later thermal cycles), and there are less secondary contaminants to interact with the salts, the ELP will more readily precipitate. As a result, if salts are added too quickly, they may become physically trapped by aggregating proteins, which effectively reduces the salt concentration of the solution and limits further protein precipitation. Thus, the salt should be added in three small batches to ensure they have sufficient time to homogenously distribute through the solution. As a final note, variations to the ELP backbone, either through further modifications to the guest residue of the elastin-like region or changes to the bio-active region can significantly impact the LCST behavior. Consequently, to ensure optimal protein yields across protein variants, it is crucial to optimize the pH, salt concentration, and salt type (e.g., monovalent or divalent) for the cold and hot spins.
Running SDS-PAGE upon protocol completion is recommended as it can be used to easily determine if significant ELP loss occurs during any of the purification steps. Briefly, if ELP is detected in the supernatant following a hot spin, then the protein is not being effectively precipitated. Similarly, if ELPs are identified in a sample of solubilized pellet following a cold spin, then the protein is not being effectively dissolved.
ELP hydrogels offer many advantages over synthetic or naturally-derived materials. Specifically, the use of the amine-reactive crosslinker THPC affords a low-cost, simple, and tunable mechanism of protein crosslinking. However, there are distinct limitations within the crosslinking protocol that should be noted. THPC is oxygen sensitive, and if stored under improper conditions, it can quickly deteriorate in reaction efficiency. In addition, due to its reactivity with primary amines, THPC may react with surrounding proteins in media or those on the cell surface that are rich in amines. Therefore, when forming ELP hydrogels, it is recommended to avoid media contamination with the cell pellet to reduce possible exogenous protein cross-reactivity and thus, a reduction in crosslinking efficiency. Finally, this crosslinking mechanism precludes the bio-active region sequence to those containing no lysine residues and thus, limits potential integration of some cell-adhesive motifs (e.g., IKVAV34). To address these limitations, modifications to the ELP backbone with azide and bicyclononyne (BCN) reaction partners allows for bio-orthogonal crosslinking, as previously described27.
It should be noted that the ELP LCST behavior plays an important role in dictating hydrogel microstructure. At temperature regimes above the LCST, ELPs precipitate out of solution leading to the formation of protein-rich and protein-deficient phases that can influence matrix porosity and crosslinking efficiency of the matrix9. Because most cell culture experiments are conducted at physiologically relevant temperatures (~37 °C) above the ELP LCST, these effects should be considered. For the hydrogels to effectively crosslink and form an interconnected protein network, the primary amine from the lysine must be physically accessible to the THPC crosslinker. If the ELP aggregation occurs before reaching sufficient crosslinking, ELPs trapped within the protein-rich phase may be inaccessible and thus unable to participate in crosslinking. To address this limitation, our protocol requires an initial 15 min crosslinking period at room temperature, which allows for preliminary crosslinking of the hydrogel before the ELP undergoes its thermal phase transition. This room temperature incubation is followed by an additional 15 min incubation at 37 °C to finalize hydrogel crosslinking. This procedure is critical for sufficient crosslinking and robust, reproducible gelation of the ELP material.
In conclusion, recombinant protein hydrogels fabricated using ELP offer exceptional tunability of the protein sequence and therefore the 3D cell microenvironment. ELP polymers have been shown to be expressible in high yields, easily purified owing to their LCST behavior, and biocompatible in a wide variety of in vitro and in vivo systems. The use of E. coli as a recombinant host provides a simple and inexpensive procedure that gives rise to near perfect control of polymer molecular weight and functionality. In conjunction, this technique allows for robust tunability and reproducibility of the hydrogel platform allowing for the culture of a wide range of cell types in 3D. Finally, this ELP hydrogel platform is amenable to many downstream biochemical assays including qRT-PCR, Western blot, DNA extraction, and cell immunostaining9.