Polyhydroxyalkanoates (PHAs) are natural polymers, primarily produced by bacteria, which are prized in drug delivery systems due to their biocompatibility, biodegradability, modifiability, and compatibility with hydrophobic drugs. In this review, formulation methods and applications of PHA nanocarriers in drug delivery are discussed, alongside the challenges of their usage and their solutions.
In the past decade, PHA-based nanoparticles as drug carriers have garnered significant attention for treating various diseases, owing to their potential to improve existing drug delivery systems via the design of novel dosage forms. Such formulations could have a better treatment outcome than conventional therapy due to their promising physicochemical properties as mentioned earlier [[18]], including (i) the ability to overcome the solubility of hydrophobic drugs, (ii) being readily manipulated for active targeting, (iii) the stabilization of chemotherapeutic agents, (iv) full biocompatibility and non-immunogenicity, and (v) superior pharmacokinetics and pharmacodynamics compared to free drug therapy [[19],[20],[21],[22],[23]]. However, US Food Drug Administration (FDA)-approved PHA-based nanomedicines for treatment are unavailable. PHA and nanotechnology-based therapies are still in the experimental stages, and clinical trials are significantly lagging.
PHA-based nanoparticles have been explored for the encapsulation of a wide range of therapeutic agents, including anticancer agents, antibiotics, hormones, and vaccines [[24],[25]]. Different formulation strategies have been explored to produce PHA nanoparticles, including emulsion solvent evaporation techniques (i.e., oil-in-water (O/W) single emulsion, and water-in-oil-in-water (W/O/W) double emulsion), nanoprecipitation, dialysis, and in situ polymerization techniques [[26],[27],[28],[29]] as summarized in Table 1. The selection of the formulation approach mainly depends on the intended particle size, morphology, and solubility of the target drug and the polymer. The emulsion solvent evaporation method has been utilized the most to produce PHA-based nanoparticles because this technique eases control of the processing parameters and allows encapsulation of both hydrophobic and hydrophilic drugs [[30]]. Generally, the drug is either dissolved or emulsified in the oil phase, then further emulsified in the continuous aqueous phase. This is followed by solvent evaporation to allow the hardening of the particles. The particles are then washed with distilled water, collected via centrifugation, and freeze-dried for long-term storage [[31]].
For instance, in a recent study, Hu and co-workers produced poly(3-hydroxybutyrate-co-3-hydroxyvalerate-co-3-hydroxyhexanoate) (PHBVHHx) nanoparticles loaded with immunosuppressant drug azathioprine for the potential treatment of systemic lupus erythematosus using the emulsion solvent technique. The particles not only had acceptable toxicity and slow clearance from kidneys, but they also exhibited a higher therapeutic effect compared to polylactic acid (PLA) nanoparticles when tested in a murine systemic lupus erythematosus model [[32]]. Similarly, Xiong et al. reported that poly(3-hydroxybutyrate) (PHB) and poly(3-hydroxybutyrate-co-12 mol% 3-hydroxyhexanoate) (PHBHHx) nanoparticles with a size range of 160-250 nm loaded with rhodamine B isothiocyanate (a lipid-soluble dye) deeply penetrated macrophages and prolonged drug release to about 20 days compared to its PLA counterpart which took about 15 days. This proves that PHA-based nano-systems can provide a slower drug release with an enhanced therapeutic index compared to PLA nanoparticles that have been well-studied as a drug control release system.
The surface of PHA nanoparticles can also be functionalized to enhance the localization of the particles in the vicinity of the cells. For example, curcumin-loaded and conjugated with targeting ligand concanavalin A in poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHx) nanoparticles (average size of 228 ± 5 nm) showed enhanced cellular uptake and apoptotic activity in breast cancer cells compared to the non-functionalized nanoparticles [[33]]. A similar higher in vitro cellular uptake was reported with etoposide (an antineoplastic agent)-loaded poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHx) nanoparticles functionalized with folic acid in HeLa cells [[34]]. As anticipated, P(3HV-co-4HB)-b-mPEG, an amphiphilic poly(3-hydroxyvalerate-co-4-hydroxybutyrate) and polyethylene glycol nanoparticle, enhanced the apoptotic activity of the encapsulated cisplatin compared to the free drug-treated group using a DU145 prostate cancer cell line [[35]]. Thus, these findings merit that PHA nanoparticles, like other polymeric nanoparticles, are suitable for targeted drug delivery systems when conjugated with targeting moieties.
On the other hand, a common drawback of PHB nano-delivery systems, especially those using scl-PHB, is the rapid release of the encapsulated drugs. However, this problem can be mitigated by conjugating the drug molecule to the PHB polymer to slow the drug release [[36]]. Additionally, the rapid release of scl-PHB can be altered by converting it into PHB glyoxylate via ozonolysis for a slow release of drugs possessing primary amine groups [[37]]. Hence, the development of PHA-drug conjugates opens a new window for novel slow-release drug delivery therapies.
Similar to other colloidal systems, PHA nanoparticles also suffer the disadvantage of poor drug loading [[38]]. For instance, a drug loading of less than 30% has been reported in various studies [[30],[35],[39],[40],[41],[42],[43]]. As a solution, the strategies reported for other polymers such as PLGA can be used as a guideline to increase the drug loading of PHA-based nanoparticles. An extensive review of strategies to increase the drug loading of polymeric particles can be found at [[30]] and [[44]].
Polymer |
Drug |
Size (nm) |
Drug loading (%) |
Formulation Method |
Key Findings |
Ref |
Poly(3-R-hydroxyalkanoate) |
Calcein and Nile red |
155 |
- |
Nanoprecipitation |
Unsaturated PHA is suitable to make controlled release nanomedicine. |
[[45]] |
Poly(3-hydroxybutyrate-co-3-hydroxyvalerate-co-3-hydroxyhexanoate) (PHBVHHx) |
Azathioprine |
95.7 |
- |
Modified emulsion |
The particles have acceptable toxicity and slow clearance from kidneys, with a higher therapeutic effect than polylactic acid (PLA) nanoparticles when tested in a murine systemic lupus erythematosus model. |
[[32]] |
Poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHx) |
Curcumin |
273 ± 84 |
15–30 |
Solvent evaporation |
Lyophilization is suitable for preserving the nanoparticles at 4°C. The particles had high apoptotic activity and localization into MDA-MB-231 cells. |
[[33]] |
Poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHX) |
Etoposide |
180–1500 |
2.92–8.77 |
Modified solvent evaporation |
Folic acid-conjugated nanoparticles have higher selectivity to cancer cells than fibroblast cells. |
[[34]] |
Poly(3-hydroxyvalerate-co-4-hydroxybutyrate) |
Cisplatin |
155 ± 5 |
9.58 ± 1 |
Emulsification–solvent evaporation |
Cisplatin-loaded PHA nanoparticles accumulated in tumour cells and showed significant tumour deterioration compared to free drug treatment. |
[[35]] |
Poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) |
Nile red |
166–426 |
- |
Oil-in-water emulsion |
The nanoparticles penetrated the skin of the BALB/c mouse model without adverse effects. |
[[46]] |
Poly (3-hydroxybutyrate-co-12 mol% 3-hydroxyhexanoate) (PHBHHx) and Poly (3-hydroxybutyrate-co-5 mol% 3-hydroxyhexanoate) (PHBV) |
TGX-221 |
195–220 |
8.5–8.8 |
Modified emulsification/solvent diffusion |
The encapsulation of TGX-221 in PHA nanoparticles could mitigate the poor bioavailability and limited in vivo half-life of the TGX-221. |
[[39]] |
Poly-3-hydroxybutyrate-co-5 mol% 3-hydroxyvalerate (PHBV-S), poly-3-hydroxybutyrate-co-11 mol% 3-hydroxyvalerate (PHBV-11) and poly-3-hydroxybutyrate-co-15 mol% 3-hydroxyvalerate (PHBV-15) |
Ellipticine |
184–283 |
- |
Modified emulsification–solvent evaporation |
The particles showed no inhibition of the A549 cancer cell line at various tested concentrations (i.e., 250.0, 62.5, and 15.6 μg/mL).
|
[[47]] |
Poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHx) |
Rapamycin |
200 |
8.47–8.52 |
Emulsification–solvent evaporation |
The particles showed an efficient entrapment of 91.9% and a sustained release of rapamycin for almost 10 days. Cellular uptake of PEG200 end-capped nanoparticles was significantly higher than that of non-PEG nanoparticles in a human prostate cancer cell line and a murine macrophage cell line. |
[[40]] |
Polyhydroxybutyrate, poly(hydroxybutyrate-co-hydroxyvalerate) P(HB-HV) with 12 and 50% HV |
5,10,15,20-Tetrakis(4-hydroxy-phenyl)-21H, 23H-porphine |
169.0–211.2 |
0.91–46.64 |
Emulsification-diffusion |
The particles showed a concentration and time-dependent photocytotoxicity in a human colon adenocarcinoma cell line.
|
[[48]] |
Poly(3-hydroxyoctanoate-co-3-hydroxyhexanoate) (PHOHHx) |
- |
44–90 |
- |
Dialysis |
A series of diblock copolymers of PHOHHx with poly(ethylene glycol) (PEG) were synthesized using “click” chemistry and assembled into micelles for drug delivery. |
[[29]] |
Poly(3-hydroxybutyrate-co-3-hydroxyvalerate) P(3HB-co-3HV) or poly(3-hydroxybutyrate-co-4-hydroxybutyrate) P(3HB-co-4HB) |
Thymoquinone |
112–162 |
- |
Modified emulsification–solvent evaporation |
The chemical combination of PHA copolymers and mPEG-based nanoparticles was nontoxic and biocompatible to prenatal rat neuronal hippocampal and NIH/3T3 fibroblast cells in vitro. |
[[49]] |
Polyhydroxybutyrate (PHB) |
NuBCP-9 |
126 ± 8 |
- |
Double emulsion solvent evaporation |
PEG-conjugated PHB nanoparticles showed a sustained release of NuBCP-9 for up to 26 days and efficient cellular uptake in a time-dependent manner in MCF-7 cells. A 90% tumour regression was seen when particles were administered intraperitoneally twice a week for three weeks in an Ehrlich syngeneic mouse model. |
[[50]] |
Polyhydroxybutyrate (PHB)
|
Nile red |
- |
- |
Oil-in-water emulsion solvent evaporation |
PHB functionalized with tumour-specific ligand nanoparticles showed a specific affinity to MDA-MB-231 breast cancer cells. |
[[51]] |
Poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHx) |
Rhodamine B isothiocyanate |
100–200 |
- |
Oil-in-water emulsion |
The recombinant human a1-acid glycoprotein or recombinant human epidermal growth factor functionalized nanoparticles were taken up by macrophages and hepatocellular carcinoma cells. |
[[52]] |
Poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) |
- |
133–300 |
- |
Miniemulsification and emulsion/solvent evaporation |
An increase of the polymer concentration led to a larger particle size due to a change in viscosity. |
[[53]] |
Poly([R,S]-3-hydroxybutyrate) (PHB) |
Doxorubicin and sorafenib |
199.3–250.5 |
2.6–8.4 |
Nanoprecipitation |
Co-encapsulation of dual anticancer drugs was achieved. A sustained and faster drug release was observed for doxorubicin and sorafenib, respectively. |
[[41]] |
Poly(hydroxioctanoate-co-hexanoate) |
- |
63 ± 4 |
- |
Emulsion-solvent evaporation |
The particles interacted with pulmonary surfactant proteins and lipids, which may limit the use of PHA for pulmonary drug delivery. |
[[54]] |
Polyhydroxyalkanoate (PHA) |
- |
145–159 |
- |
Oil-in-water emulsion |
The PHA nanoparticles showed antibacterial activity against S. aureus, S. pneumoniae, E. coli, K. pneumoniae, and P. aeruginosa. |
[[55]] |
Poly(3-hydroxybutyrate-co-3-hydroxyoctanoate) (P(HB-HO)) |
Doxorubicin |
240 |
29.6 |
Water-in-oil-in-water solvent extraction/evaporation |
Doxorubicin-loaded folate-mediated nanoparticles were readily internalized by HeLa cells in vitro. |
[[42]] |
Polyhydroxybutyrates (PHB) |
Concanavalin-A and etoposide |
239.43 ± 5.25 |
- |
Multi-emulsion |
Iron oxide particles were successfully coated with PHB. The cytotoxicity of these magnetic PHB particles were reported against cancer and non-cancer cells. |
[[56]] |
Poly(hydroxybutyrate-co-hydroxyvalerate) (PHBV) |
Fingolimod |
250 |
0–22.5 |
Single and double evaporation |
The optimal preparation of PHBV nanoparticles required a polymer concentration of 1.32%, a PVA concentration of 0.42%, and 5 mg of the drug. |
[[43]] |
Note: ‘-’ indicates the value was not reported.
Biocompatibility and cytotoxicity are major concerns for PHA applications as medical tools. Although the biocompatibility of PHAs is well-understood, the cytotoxicity should be minimized with caution by ensuring the purity of PHA employed in medical tool development. Repeated dissolving and precipitation of PHA in downstream processes of microbial PHA production systems are needed to guarantee the high purity of PHA [[104]]. However, residual organic solvents such as chloroform for PHA extraction and methanol for PHA precipitation could be a health threat if not removed completely prior to in vivo applications. The cytotoxicity of chloroform is attributed to its ability to modify the properties of the cell membrane lipid matrix that may lead to cell death [[105],[106],[107]]. Methanol is cytotoxic due to its inhibitory effect on cell proliferation at a concentration of more than 10% [[108]]. Complete removal can be achieved by ensuring the complete evaporation of residual solvents from the PHA pellets, considering the volatile nature of these solvents, followed by proper washing. Apart from chemical extraction, PHA can be extracted biologically by feeding PHA-harboring microbial cells to a mealworm species (Tenebrio molitor) that discharges PHA as waste [[109]].
Microbial production of PHA involves mainly Gram-negative bacteria, with Cupriavidus necator (also known as Ralstonia eutropha) as the standard PHA-producing bacteria among them. The endotoxins constitute lipopolysaccharides (LPS), heat-resistant components located in the outer cell membrane of Gram-negative bacteria, which are responsible for inflammatory reactions in biomedical applications of biomaterials. LPS are liberated during PHA extraction steps, where the cell biomass is lysed. The LPS then contaminates the resulting PHA and are carried along to the precipitation step, thus remaining on the resulting PHA pellets [[104],[110],[111],[112]]. The proper and efficient removal of endotoxins is necessary to assure in vivo applicability, and common removal methods include using sodium hydroxide or hydrogen peroxide [[113],[114]]. Alternatively, endotoxin-free PHA can be obtained by using Gram-positive bacteria for production instead, owing to the inability of Gram-positive bacteria to produce LPS. Bacillus is a popular choice, given its promising PHA yield and less stringent requirements for fermentation conditions [[115],[116]].
Although PHAs are biocompatible, some of their physicochemical properties hinder wider use in several applications. Poly(3-hydroxybutyrate) [P(3HB)] and Poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] are the most studied PHAs for numerous biomedical applications [[25],[117],[118],[119],[120]]. The employment of homopolymer P(3HB) as a drug delivery device is discouraging due to its inherently poor thermal stability that leads to limited processibility and uncontrollable drug release kinetics [[121]]. The incorporation of a 3-hydroxyvalerate (3HV) monomer provides better flexibility and strength, with reduced chain packing and toughness in the resulting copolymeric P(3HB-co-3HV) [[122],[123],[124],[125],[126]]. P(3HB-co-3HV) is attractive as a drug delivery agent, as the higher molar fraction of 3HV in the copolymer contributes to a more amorphous structure that favors drug release [[127],[128]]. Additionally, the incorporation of a second or even third monomer to form a copolymer or terpolymer also leads to lower crystallinity which is a desirable characteristic for PHA-based implants that require sufficient biodegradability [[129]]. In addition to biodegradability, enhanced mechanical properties can also be achieved to provide support in arteries as a stent in angioplasty [[130]]. However, PHAs have poor compatibility with therapeutic agents, which results in a low encapsulation efficiency due to their hydrophobicity, as mentioned earlier. Incorporation of hydrophilicity is generally done by functionalizing PHA with polar functional groups, or by block/graft copolymerization of PHA with hydrophilic components such as poly(ethylene glycol) [[49],[131]].
Despite the excellent potential of PHAs, their high selling price is a major drawback when considering their use in medical applications. As the carbon sources employed in PHA manufacturing contribute to 30‒40% of the overall production costs, the employment of waste in substitution of defined carbon sources was attempted to make PHA more affordable and economically competitive [[132],[133]]. With increasing emphasis on sustainability, waste plant oils are gaining great interest [[134]]. One concern in using such PHAs for biomedical applications is that the residual oils will adhere to bacterial biomass, then be carried forward to subsequent downstream processing. Residual oil removal is usually carried out using non-polar organic solvents such as hexane, which has a polarity index of 0.1. The cell biomass must be washed repeatedly with clean water after primary washing with solvents for complete removal [[135],[136]]. Alternately, residual oil removal can also be done using supercritical CO2 and CO2-expanded ethanol. The supercritical CO2 method has been shown to remove impurities of more than 70 wt% from P(3HB). In contrast, more than 93 wt% of residual oils were removed by adding a small volume of ethanol in the presence of CO2, which lowered the pressure requirement for the oil removal process [[137]]. As CO2 and ethanol are easily recyclable and relatively harmless, the employment of organic and hazardous solvents can be minimized.
Since the discovery of PHAs in 1888 by Martinus W. Beijerinck, the polymers have been extensively studied for the last eight decades due to academic interest [[138]]. The introduction of eco-friendly bio-based products as alternatives to conventional plastics brought the term ‘bioplastics’ to public attention. Although PHAs have generated a lot of interest in the last few decades due to their material properties, biocompatibility, and sustainability, the selling price of PHAs is still the main determining factor for commercialization [[139]]. The development of PHA production strategies is a continuous effort to bring about a higher PHA yield and economic attraction. Designing, evaluating, and optimizing PHA-based formulations for pharmaceutical and therapeutic applications still require more studies before their wide implementation in pharmaceutical industries due to the disadvantages resulting from their material properties [[140],[141]]. Although there is still much to be explored, emerging knowledge is turning PHAs into convenient, high-performance, and economically competitive polymers that can be widely accepted and implemented for medication in the foreseeable future.This entry is adapted from the peer-reviewed paper 10.3390/nano12010175