Purification of the human fibroblast growth factor 2 using novel animal-component free materials
Introduction
The glycosaminoglycan heparin is a highly sulphated polysaccharide which is important for various biological interactions [1], [2]. Heparin is known for its function as an inhibitor in the coagulation cascade to maintain blood flow in the vasculature system [3]. Based on this property, heparin has seen widespread clinical use [4], [5]. The biological activities of heparin are associated with its interaction with various proteins, which have led to its use in protein purification in biotechnological applications [6], [7]. Diverse biologically active heparin-binding proteins, such as the human fibroblast growth factor 1 (hFGF-1) [8], hFGF-2 [9], [10], the human bone morphogenic protein 2 (hBMP-2) [11], the serine protease thrombin [12], and the glycoprotein anti-thrombin III (ATIII) [13], can be successfully purified by heparin affinity chromatography in a very effective and simple process [7], [14], [15], [16]. However, heparin is an animal-derived material, which is most frequently obtained from bovine or porcine tissue. Animal-based components are ethically problematic and carry the risk of virus contaminations [14], requiring strict quality controls and the validation of effective good manufacturing practice (GMP) implementation. Adequate animal-free components are therefore of considerable interest.
There are two options to replace conventional heparin in affinity chromatography. One option is to use chemically synthesized heparin [17], [18], chemoenzymatically synthesized heparin [17], [19], or bioengineered recombinant heparin, e.g. from genetically modified Chinese Hamster Ovary (CHO) cells [20]. Such bioengineered heparins have been applied in pharmaceuticals and for structure analysis but are very expensive. To our knowledge, there have not been studies on the use of bioengineered heparin for purification methods to date.
The second option is the use of animal-component free chromatographic methods, applying MMC and pseudo-affinity chromatography as an alternative to heparin affinity chromatography. Ligands of MMCs are characterized by a multimodal functionality compared to traditional single-mode chromatographic ligands [21], [22]. These materials are characterized by the availability of different ligands in one material. Various functional groups can build up different types of interactions (ionic interactions, hydrogen bonds, Van-der-Waals interactions) which can lead to a high affinity to different proteins, enabling a broad range of applications [9], [23], [24], [25]. MMCs are salt-tolerant due to their hydrophobic functionalities. This behaviour shortens the purification process time through fewer desalting steps and thus reduces the purification costs. This is advantageous as each additional purification step is associated with protein loss and higher purification costs [22], [25].
The pseudo-affinity chromatography is related to the affinity chromatography but is based on pseudo-specific ligands which are chemically synthesized. In contrast to the ligands in the traditional affinity chromatography, the ligands of the pseudo-affinity chromatography are easier and cheaper to produce and are more robust to chemical or biochemical degradation [26].
Several groups have already tested animal-component free materials to purify heparin-binding proteins [25], [27], [28], [29]. They all have in common that the purified proteins are produced as inclusion bodies. These inclusion bodies have already a purity of 80 % which makes further purification steps easier.
In this study we produced the cytokine hFGF-2 in recombinant Escherichia coli (E. coli) in a soluble form. After cell disruption and centrifugation, the experiments were performed with the soluble cell fraction. Eight different animal-component free materials (different mixed-mode and pseudo-affinity chromatography materials) were tested in bead-based column chromatography or membrane adsorbers technology (Table S1).
Section snippets
Plasmid, strain, cultivation method
The E. coli strain BL21(DE3) (Novagen, Germany) with the plasmid pET29(+)-hFGF-2 was constructed by Hoffmann et al. [30]. The cultivation method for the production of hFGF-2 has been previously described by Li et al. [31].
Cell disruption
Cell pellets were resuspended in 15 mL lysis buffer (25 mM phosphate buffer, 100 mM NaCl, 3 mM DTT, 1 mM EDTA, pH 7.5) per gram cell pellet and disrupted with a high pressure homogenizer (M-110L, Microfluidics, USA) at 9000 psi in 10 cycles. After centrifugation the
Results and discussion
All chromatographic techniques were tested with the soluble cell fraction, which was obtained after cell disruption and centrifugation. The relative content of hFGF-2 in the overall protein content was around 12 %, the remaining 88 % were E. coli host cell proteins. The established method [9] consisted of three chromatographic steps (Fig. 1A), a cation exchange chromatography as a capture step, the heparin affinity chromatography as an intermediate purification step and an anion exchange
Conclusion
In conclusion, we demonstrated two animal-component free chromatographic purification materials for the purification of the growth factor hFGF-2. The exchange of the heparin in the affinity chromatography through the MMCs HiTrapTM CaptoTM MMC and ForesightTM NuviaTM cPrimeTM purified the hFGF-2 up to 90 % with a yield and recovery of 85 %. Additionally, the purified protein was also endotoxin free and bioactive.
This bead-based column chromatography can be adapted to other heparin-binding
Funding
This work was supported by Forschergruppe the research group “Graded Implants FOR2180” and the Cluster of Excellence “Rebirth” EXC62, both German Research Foundation (DFG).
Ethical approval
No studies with human participants or animals were performed by any of the authors for this study.
CRediT authorship contribution statement
Svenja Nicolin Bolten: Conceptualization, Writing - original draft, Methodology, Investigation, Writing - review & editing. Anne-Sophie Knoll: Validation, Investigation. Zhaopeng Li: Validation, Writing - review & editing. Pia Gellermann: Validation. Iliyana Pepelanova: Validation. Ursula Rinas: Supervision. Thomas Scheper: Supervision, Resources, Writing - review & editing.
Declaration of Competing Interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
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