| Literature DB >> 25720989 |
Nina Dinjaski1, M Auxiliadora Prieto2.
Abstract
The development of innovative medicines and personalized biomedical approaches calls for new generation easily tunable biomaterials that can be manufactured applying straightforward and low-priced technologies. Production of functionalized bacterial polyhydroxyalkanoate (PHA) nanobeads by harnessing their natural carbon-storage granule production system is a thrilling recent development. This branch of nanobiotechnology employs proteins intrinsically binding the PHA granules as tags to immobilize recombinant proteins of interest and design functional nanocarriers for wide range of applications. Additionally, the implementation of new methodological platforms regarding production of endotoxin free PHA nanobeads using Gram-positive bacteria opened new avenues for biomedical applications. This prompts serious considerations of possible exploitation of bacterial cell factories as alternatives to traditional chemical synthesis and sources of novel bioproducts that could dramatically expand possible applications of biopolymers. FROM THE CLINICAL EDITOR: In the 21st century, we are coming into the age of personalized medicine. There is a growing use of biomaterials in the clinical setting. In this review article, the authors describe the use of natural polyhydroxyalkanoate (PHA) nanoparticulates, which are formed within bacterial cells and can be easily functionalized. The potential uses would include high-affinity bioseparation, enzyme immobilization, protein delivery, diagnostics etc. The challenges of this approach remain the possible toxicity from endotoxin and the high cost of production.Entities:
Keywords: Depolymerase; Functionalized polyhydroxyalkanoates; Granule associated proteins; Phasins; Synthase
Mesh:
Substances:
Year: 2015 PMID: 25720989 PMCID: PMC7106125 DOI: 10.1016/j.nano.2015.01.018
Source DB: PubMed Journal: Nanomedicine ISSN: 1549-9634 Impact factor: 5.307
Figure 1Polyhydroxyalkanoates (PHAs) bacterial biopolyesters, synthesized from renewable sources and characterized by biodegradability and biocompatibility.
Figure 2Classification of polyhydroxyalkanoates (PHAs) according to monomer size, functional substituents, polymer structure and protein functionalization.
Figure 3Pseudomonas putida KT2440 mcl-PHA granule producing cell with the schematic representation of PHA granule structure composed of a PHA core coated with phospholipid monolayer where granule-associated proteins GAPs (phasins, synthases, depolymerase, ACS1) are embedded or attached (modified from ).
Figure 4Schematic representation of the currently used strategies for PHA functionalization centered around added-value PHA production. In vivo PHA modification based on peptide functionalization of PHA nano-beads using GAPs for recombinant protein anchoring to the PHA granule or nonspecific binding and in vivo chemical modification through incorporation of functional group in the side chain of the polymer applying metabolic engineering and systems biology approach. Similarly to in vivo, in vitro approach for peptide functionalization can be based on the use of GAPs or nonspecific binding, while the underlying principle of in vitro chemical modification might be based on polymer synthesis or modification.
Summary of the developments on PHA nanobead protein functionalization for various applications.
| PHA | Functionalization | GAP | Bacterial strain | Ref. | |
|---|---|---|---|---|---|
| Diagnostics | PHB | Mouse interleukin 2 IL2/myelin oligodendrocite glycoprotein MOG | PhaP phasin PhaC synthase | ||
| PHA | EFG/RFG/Severe acute respiratory syndrome corona virus SARSCoV envelop protein | PHA depolymerase | |||
| PHB | Tuberculosis antigens, ESAT6, CFP10, and Rv3615c | PhaC synthase | |||
| PHB | Anti-β-galactosidase single-chain antibody variable fragment scFv | PhaC synthase | |||
| Vaccines | PHB | PhaC synthase | |||
| PHB | Hepatitis C virus core antigen HCc | PhaC synthase | |||
| Drug delivery | PHBHHx | Mannosylated human α1-acid glycoprotein (hAGP)/human epidermal growth factor (hEGF) | PhaP phasin | ||
| PHB | RGD | PhaC synthase | |||
| PHB/PHBHHx | Rhodamine B isothiocyanate RBITC | Non | |||
| PHB | Rifampicin | Non | |||
| PHBHHx | Triamcinolone Acetonide | Non | |||
| PHB | Lomustine CCNU | Non | |||
| PHBHHx | Heparzine-A | Non | |||
| PHB | Diclofenac, dexamethasone | Non | |||
| PHBHHx | Etoposide and attached folic acid | Non | |||
| PHBHHx | Platelet-derived growth factor-BB (PDGF-BB) | Non | |||
| Cell targeting | PHBHHx | Polyethylenimine coating | Non | ||
| Imaging | PHB | GFP/HcRed | PhaC synthase/PhaP phasin | ||
| PHO | GFP | PhaF phasin | |||
| PHB | Inorganic material binding peptide, antibody binding ZZ domain | PhaC synthase | |||
| Insecticide | PHO | Cry1Ab | PhaF phasin | ||
| Bioseparation | Immunoglobulin G (IgG) binding ZZ domain of | PhaC synthase | |||
| PHB | ZZ | PhaC synthase | |||
| PHB | Streptavidin | PhaC synthase | |||
| Protein purification | PHB | EGFP/Maltose binding protein MBP/β-galactosidase ( | PhaP phasin | ||
| PHB | GFP, LacZ | PhaP phasin | |||
| PHB | Intein self-cleaving affinity tag, EGFP, MBP, LacZ | PhaP phasin | |||
| Enzymes | mclPHA | PhaC synthase | |||
| PHB | α-amylase variant (TermamylTM) | PhaC synthase | |||
| PHB | Organophosphohydrolase OpdA | PhaC synthase | |||
| PHB | PhaA-PhaB | PhaC synthase | |||
| Endotoxin removal | PHB | Lipopolysaccharide binding protein | PhaP phasin |
Comparison of PHA nanoparticles in vitro and in vivo production process, their applications and costs.
| Ref. | |||
|---|---|---|---|
| Production and processing | Production by bacteria | Synthetic production | |
| Use of renewable sources for production | Harsh chemical needed for polymer isolation and particle production | ||
| Simultaneous production and functionalization | Functionalization posterior to nanobead production | ||
| Nanobead assembly and disassembly cannot be tightly controlled | Tight control over bead assembly and disassembly | ||
| Competition of recombinant and wild type GAPs | Functionalization with target protein only, no other GAPs | ||
| Particle size can be controlled by biotechnological production process | Tight control over particle size | ||
| Immobilized protein concentration variation might represent challenge | Tight control over immobilized protein concentration | ||
| In the case of Gram- strains endotoxins cannot be removed, while if produced in Gram+ endotoxins absent | Endotoxin removal possible and needed | ||
| Applications | Suitable for environmental applications; Insecticide delivery | Suitable for biomedical applications; Drug delivery | |
| Protein purification | Diagnostics | ||
| Endotoxin removal | Vaccines | ||
| Production cost | Total production cost includes | Higher production costs compared to |
Figure 5In vivo immobilization of fusion proteins to bioplastics by BioF tag. The procedure consists of: 1, the fermentation in P. putida under optimal PHA production conditions; 2, 3, isolation of the granules carrying the BioF-proteins fusions from the crude cell lysate by a simple centrifugation step; 4, release of fusion proteins via detergent treatment (modified from ).
Comparison of synthetic and natural polyesters production, processing, properties and application.
| Synthetic polyesters | Bacterial polyesters (PHA) | Ref. | |
|---|---|---|---|
| Production and processing | Bio-production of LA and chemical synthesis of PLA, PLGA | Completely biosynthesized | |
| No possibility of | |||
| Use of harsh chemicals for production | Production from renewable sources | ||
| Difficulty to scale-up | Similar to bioprocesses for PHA production; Certain difficulties to scale-up | ||
| Production cost comparable with conventional plastics like PET | High cost of production; at least twice that of PLA | ||
| High risk due to flammable and toxic solvents | Low risk level | ||
| Production completed within days | Production duration 1-2 weeks | ||
| Endotoxin contamination less probable due to synthetic origin | Endotoxins can be efficiently removed; Use of Gram+ strains allows endotoxin free production | ||
| Properties | Lower number of copolymers that can be produced; Only | More than 150 monomeric building blocks for polymer design | |
| Approved by FDA and European Medicine Agency as drug delivery system | Not approved by FDA as drug delivery system | ||
| Low drug loading | No limitations regarding drug loading | ||
| Protection of drug from degradation | Protection of drug from degradation | ||
| Biodegradable, biocompatible, low cytotoxicity | Biodegradable, biocompatible, low cytotoxicity | ||
| Material properties poor, could be adjusted by regulating | Good thermomechanical properties from brittle, flexible to elastic, fully controllable, easy processability | ||
| Degradation rate can be controlled | Degradation rate can be controlled | ||
| Drug delivery kinetics can be controlled | Drug delivery kinetics can be controlled | ||
| Easy particle size control | Size of | ||
| Application | Wind variety of biomedical applications | Applicable to a range of diseases | |
| Lowering pH at the site of implantation that might lead to sterile sepsis | No detected side effect of PHA degradation | ||
| Best chance for clinical application due to FDA approval. Packaging, printing, coating, yet limited by | Almost all areas of conventional plastic industry, limited by current higher cost and availability |