Polyhydroxyalkanoates
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Polyhydroxyalkanoates or PHAs are polyesters produced in nature by numerous microorganisms, including through bacterial fermentation of sugars or lipids.[1] When produced by bacteria they serve as both a source of energy and as a carbon store. More than 150 different monomers can be combined within this family to give materials with extremely different properties.[2] These plastics are biodegradable and are used in the production of bioplastics.[3]
They can be either thermoplastic or elastomeric materials,[4] with melting points ranging from 40 to 180 °C.[citation needed]
The material properties and biocompatibility of PHA can also be changed by blending, modifying the surface or combining PHA with other polymers, enzymes and inorganic materials, expanding the range of applications.[5][6]
Biosynthesis
[edit]
To induce PHA production in a laboratory setting, a culture of a micro-organism such as Cupriavidus necator can be placed in a suitable medium and fed appropriate nutrients so that it multiplies rapidly. Once the population has reached a substantial level, the nutrient composition can be changed to force the micro-organism to synthesize PHA. The yield of PHA obtained from the intracellular granule[further explanation needed] inclusions can be as high as 80% of the organism's dry weight.[citation needed]
The biosynthesis of PHA is usually caused by deficiency conditions (e.g. lack of macro elements such as phosphorus, nitrogen, trace elements, or lack of oxygen) and the excess supply of carbon sources.[7] However, the prevalence of PHA production within either a mono-culture or a set of mixed-microbial organisms can also be dependent on overall nutrient limitation, not just macro elements. This is especially the case in the 'feast/famine' cycle method for induction of PHA production, wherein carbon is periodically added and depleted to cause famine, which encourages cells to produce PHA during 'feast' as a storage method for periods of famine. [citation needed]
Polyesters are deposited in the form of highly refractive granules in the cells. Depending upon the microorganism and the cultivation conditions, homo- or copolyesters with different hydroxyalkanoic acids are generated. PHA granules are then recovered by disrupting the cells.[8] Recombinant Bacillus subtilis str. pBE2C1 and Bacillus subtilis str. pBE2C1AB were used in production of polyhydroxyalkanoates (PHA) and it was shown that they could use malt waste as carbon source for lower cost of PHA production.[9]
PHA synthases are the key enzymes of PHA biosynthesis. They use the coenzyme A - thioester of (r)-hydroxy fatty acids as substrates. The two classes of PHA synthases differ in the specific use of hydroxy fatty acids of short or medium chain length.
The resulting PHA is of the two types:
- Poly (HA SCL) from hydroxy fatty acids with short chain lengths including three to five carbon atoms are synthesized by numerous bacteria, including Cupriavidus necator and Alcaligenes latus (PHB).
- Poly (HA MCL) from hydroxy fatty acids with medium chain lengths including six to 14 carbon atoms, can be made for example, by Pseudomonas putida.
A few bacteria, including Aeromonas hydrophila and Thiococcus pfennigii, synthesize copolyester from the above two types of hydroxy fatty acids, or at least possess enzymes that are capable of part of this synthesis.
Another even larger scale synthesis can be done with the help of soil organisms. For lack of nitrogen and phosphorus they produce a kilogram of PHA per three kilograms of sugar.
The simplest and most commonly occurring form of PHA is the fermentative production of poly-beta-hydroxybutyrate [poly(3-hydroxybutyrate), P(3HB)], which consists of 1000 to 30000 hydroxy fatty acid monomers.
Industrial production
[edit]In the industrial production of PHA, the polyester is extracted and purified from the bacteria by optimizing the conditions of microbial fermentation of sugar, glucose, or vegetable oil.
In the 1980s, Imperial Chemical Industries developed poly(3-hydroxybutyrate-co-3-hydroxyvalerate) obtained via fermentation that was named "Biopol". It was sold under the name "Biopol" and distributed in the U.S. by Monsanto and later Metabolix.[10]
As raw material for the fermentation, carbohydrates such as glucose and sucrose can be used, but also vegetable oil or glycerine from biodiesel production. Researchers in industry are working on methods with which transgenic crops will be developed that express PHA synthesis routes from bacteria and so produce PHA as energy storage in their tissues. Several companies are working to develop methods of producing PHA from waste water, including Veolia subsidiary Anoxkaldnes.[11] and start-ups, Micromidas,[12] Mango Materials,[13][14] Full Cycle Bioplastics,[15] Newlight and Paques Biomaterials.[16][17]
PHAs are processed mainly via injection molding, extrusion and extrusion bubbles into films and hollow bodies.
Material properties
[edit]PHA polymers are thermoplastic, can be processed on conventional processing equipment, and are, depending on their composition, ductile and more or less elastic.[18] They differ in their properties according to their chemical composition (homo-or copolyester, contained hydroxy fatty acids).
They are UV stable, in contrast to other bioplastics from polymers such as polylactic acid, partial ca. temperatures up to 180 °C, and show a low permeation of water. The crystallinity can lie in the range of a few to 70%. Processability, impact strength and flexibility improves with a higher percentage of valerate in the material. PHAs are soluble in halogenated solvents such chloroform, dichloromethane or dichloroethane.[19]
PHB is similar in its material properties to polypropylene (PP), has a good resistance to moisture and aroma barrier properties. Polyhydroxybutyric acid synthesized from pure PHB is relatively brittle and stiff. PHB copolymers, which may include other fatty acids such as beta-hydroxyvaleric acid, may be elastic.
Applications
[edit]-
Structure of poly-3-hydroxyvalerate (PHV)
-
Structure of poly-4-hydroxybutyrate (P4HB)
Due to its biodegradability and potential to create bioplastics with novel properties, much interest exists to develop the use of PHA-based materials. PHA fits into the green economy as a means to create plastics from non-fossil fuel sources. Furthermore, active research is being carried out for the biotransformation "upcycling" of plastic waste (e.g., polyethylene terephthalate and polyurethane) into PHA using Pseudomonas putida bacteria.[20]
A PHA copolymer called PHBV (poly(3-hydroxybutyrate-co-3-hydroxyvalerate)) is less stiff and tougher, and it may be used as packaging material.
In June 2005, US company Metabolix, Inc. received the US Presidential Green Chemistry Challenge Award (small business category) for their development and commercialisation of a cost-effective method for manufacturing PHAs.[21]
There are potential applications for PHA produced by micro-organisms[2] within the agricultural,[22] medical and pharmaceutical industries, primarily due to their biodegradability.
Fixation and orthopaedic applications have included sutures, suture fasteners, meniscus repair devices, rivets, tacks, staples, screws (including interference screws), bone plates and bone plating systems, surgical mesh, repair patches, slings, cardiovascular patches, orthopedic pins (including bone.lling augmentation material), adhesion barriers, stents, guided tissue repair/regeneration devices, articular cartilage repair devices, nerve guides, tendon repair devices, atrial septal defect repair devices, pericardial patches, bulking and filling agents, vein valves, bone marrow scaffolds, meniscus regeneration devices, ligament and tendon grafts, ocular cell implants, spinal fusion cages, skin substitutes, dural substitutes, bone graft substitutes, bone dowels, wound dressings, and hemostats.[23]
References
[edit]- ^ Lu, Jingnan; Tappel, Ryan C.; Nomura, Christopher T. (2009-08-05). "Mini-Review: Biosynthesis of Poly(hydroxyalkanoates)". Polymer Reviews. 49 (3): 226–248. doi:10.1080/15583720903048243. ISSN 1558-3724. S2CID 96937618.
- ^ a b Doi, Yoshiharu; Steinbuchel, Alexander (2002). Biopolymers. Weinheim, Germany: Wiley-VCH. ISBN 978-3-527-30225-3.[page needed]
- ^ Bhubalan, Kesaven; Lee, Wing-Hin; Sudesh, Kumar (2011-05-03), Domb, Abraham J.; Kumar, Neeraj; Ezra, Aviva (eds.), "Polyhydroxyalkanoate", Biodegradable Polymers in Clinical Use and Clinical Development, John Wiley & Sons, Inc., pp. 247–315, doi:10.1002/9781118015810.ch8, ISBN 978-1-118-01581-0
- ^ Rodriguez-Contreras, Alejandra (2019-09-12). "Recent Advances in the Use of Polyhydroyalkanoates in Biomedicine". Bioengineering. 6 (3): 82. doi:10.3390/bioengineering6030082. ISSN 2306-5354. PMC 6784168. PMID 31547270.
- ^ Michael, Anne John (September 12, 2004). "Polyhydroxyalkanoates for tissue engineering". Archived from the original on January 28, 2007.
- ^ Li, Zibiao; Yang, Jing; Loh, Xian Jun (April 2016). "Polyhydroxyalkanoates: opening doors for a sustainable future". NPG Asia Materials. 8 (4): e265. doi:10.1038/am.2016.48. ISSN 1884-4057.
- ^ Kim, Y. B.; Lenz, R. W. (2001). "Polyesters from microorganisms". Advances in Biochemical Engineering/Biotechnology. 71: 51–79. doi:10.1007/3-540-40021-4_2. ISBN 978-3-540-41141-3. ISSN 0724-6145. PMID 11217417.
- ^ Jacquel, Nicolas; Lo, Chi-Wei; Wei, Yu-Hong; Wu, Ho-Shing; Wang, Shaw S. (2008). "Isolation and purification of bacterial poly(3-hydroxyalkanoates)". Biochemical Engineering Journal. 39 (1): 15–27. Bibcode:2008BioEJ..39...15J. doi:10.1016/j.bej.2007.11.029.
- ^ Wang, Yuije; Ruan, Lifang; H.F.Yu, Peter (2006). "Cloning and expression of the PHA synthase genes phaC1 and phaC1AB into Bacillus subtilis". World Journal of Microbiology and Biotechnology. 22 (22): 559–563. doi:10.1007/s11274-005-9071-7.
- ^ Ewa Rudnik (3 January 2008). Compostable Polymer Materials. Elsevier. p. 21. ISBN 978-0-08-045371-2. Retrieved 10 July 2012.
- ^ Seb Egerton-Read (September 9, 2015). "A New Way to Make Plastic". Circulate. Archived from the original on October 20, 2015. Retrieved October 23, 2015.
- ^ Martin Lamonica (May 27, 2010). "Micromidas to test sludge-to-plastic tech". CNET. Retrieved October 23, 2015.
- ^ Mango Materials selected for Phase II STTR NASA award (10. Aug 2017) BioplasticsMagazine.com
- ^ How Close Are We to Reinventing Plastic? (Dec 18, 2019) Seeker
- ^ "Full Cycle Bioplastics Turns Bacteria Waste into "Nature's Plastic"". 11 July 2019.
- ^ "Paques biomaterials website".
- ^ Provincie Drenthe (2022). "Paques Biomaterials investeert 58 miljoen in demo-installatie en fabriek in Emmen". Archived from the original on 2022-09-23. Retrieved 2022-11-16.
- ^ Cataldi, P. (July 2020). "Multifunctional Biocomposites Based on Polyhydroxyalkanoate and Graphene/Carbon Nanofiber Hybrids for Electrical and Thermal Applications". ACS Applied Polymer Materials. 2 (8): 3525–3534. arXiv:2005.08525. doi:10.1021/acsapm.0c00539. S2CID 218673849.
- ^ Jacquel, Nicolas; Lo, Chi-Wei; Wu, Ho-Shing; Wei, Yu-Hong; Wang, Shaw S. (2007). "Solubility of polyhydroxyalkanoates by experiment and thermodynamic correlations". AIChE Journal. 53 (10): 2704–14. Bibcode:2007AIChE..53.2704J. doi:10.1002/aic.11274.
- ^ "Homepage - P4SB". www.p4sb.eu. Retrieved 2017-10-26.
- ^ "The Presidential Green Chemistry Challenge Awards Program" (PDF). The Presidential Green Chemistry Challenge Awards Program: Summary of 2005 Award Entries and Recipients. Environmental Protection Agency: 8. 2005. Archived from the original (PDF) on 2012-07-08.
- ^ Amelia, Tan Suet May; Govindasamy, Sharumathiy; Tamothran, Arularasu Muthaliar; Vigneswari, Sevakumaran; Bhubalan, Kesaven (2019), Kalia, Vipin Chandra (ed.), "Applications of PHA in Agriculture", Biotechnological Applications of Polyhydroxyalkanoates, Springer Singapore, pp. 347–361, doi:10.1007/978-981-13-3759-8_13, ISBN 978-981-13-3758-1, S2CID 139827723
- ^ Chen, Guo-Qiang; Wu, Qiong (2005). "The application of polyhydroxyalkanoates as tissue engineering materials". Biomaterials. 26 (33): 6565–78. doi:10.1016/j.biomaterials.2005.04.036. PMID 15946738.
Further reading
[edit]- Mohapatra, S.; Sarkar, B.; Samantaray, D. P.; Daware, A.; Maity, S.; Pattnaik, S.; Bhattacharjee, S. (2017). "Bioconversion of fish solid waste into PHB using Bacillus subtilis based submerged fermentation process". Environmental Technology. 38 (24): 1–8. Bibcode:2017EnvTe..38.3201M. doi:10.1080/09593330.2017.1291759. PMID 28162048. S2CID 1080507.
- Mohapatra, Swati; Maity, Sudipta; Dash, Hirak Ranjan; Das, Surajit; Pattnaik, Swati; Rath, Chandi Charan; Samantaray, Deviprasad (December 2017). "Bacillus and biopolymer: Prospects and challenges". Biochemistry and Biophysics Reports. 12: 206–13. doi:10.1016/j.bbrep.2017.10.001. PMC 5651552. PMID 29090283.
Polyhydroxyalkanoates
View on GrokipediaOverview
Definition and Structure
Polyhydroxyalkanoates (PHAs) are a family of intracellular polyesters synthesized by diverse bacteria and some archaea, such as species in the genera Haloferax and Haloterrigena, as carbon and energy storage compounds under unbalanced growth conditions.[4][5] These biopolymers accumulate as discrete granules within the microbial cytoplasm when carbon sources are abundant but essential nutrients like nitrogen, phosphorus, or oxygen are limited, allowing cells to store up to 90% of their dry weight as PHAs for later mobilization.[6][4] The chemical structure of PHAs is based on repeating monomeric units of 3-hydroxyalkanoic acids, forming linear polyester chains through ester linkages between the hydroxyl and carboxyl groups.[6] The general repeating unit can be represented as:History and Discovery
The first observation of polyhydroxyalkanoate (PHA) granules occurred in 1888, when microbiologist Martinus Willem Beijerinck identified light-refractive inclusions in the cytoplasm of Bacillus species during microscopic examinations of bacterial cells.[7] These granules were initially noted as unusual cellular structures but were not chemically characterized at the time.[8] In 1926, French microbiologist Maurice Lemoigne isolated and identified the first specific PHA, poly(3-hydroxybutyrate) (PHB), from Bacillus megaterium, establishing it as a polyester composed of 3-hydroxybutyric acid monomers.[9] Lemoigne's work demonstrated that PHB accumulated as intracellular granules under nutrient-limited conditions, serving as a carbon and energy reserve.[10] Following this discovery, research interest in PHAs diminished until the mid-20th century, when studies in the 1950s and 1960s focused on microbial lipid inclusions, confirming their role as storage polymers through chemical analyses and extraction techniques developed by researchers such as Forsyth and Lundgren.[11] The 1970s oil crises sparked renewed interest in PHAs as potential biodegradable alternatives to petroleum-based plastics, prompting extensive research into scalable microbial production.[12] In 1976, Imperial Chemical Industries (ICI) in the United Kingdom initiated development of a fermentation process for PHB using Alcaligenes eutrophus (now Cupriavidus necator), culminating in a key patent for its commercial production in 1981.[13] This effort led to the launch of Biopol, the first commercial PHA copolymer, in the late 1980s, though high production costs limited widespread adoption.[14] In the 1990s, Monsanto acquired ICI's PHA technology and patents from Zeneca in 1996, pursuing plant-based production of PHB in crops like canola and soybeans to reduce costs, but abandoned these efforts by the early 2000s due to economic challenges and low yields.[12] Interest revived in the 2000s through biotechnology firms, notably Metabolix, which partnered with Archer Daniels Midland (ADM) in 2004 to develop microbial fermentation for diverse PHAs, announcing plans in 2006 for the first large-scale commercial plant with an annual capacity of 110 million pounds.[15] This marked a shift toward engineered strains and renewable feedstocks, positioning PHAs for broader industrial viability.[16]Classification
Short-Chain-Length PHAs
Short-chain-length polyhydroxyalkanoates (scl-PHAs) are a subclass of polyhydroxyalkanoates characterized by repeating monomer units containing 3 to 5 carbon atoms.[17][1] These biopolymers are typically rigid and brittle thermoplastics due to their short side chains, distinguishing them from longer-chain variants.[1] The most prevalent scl-PHAs include poly(3-hydroxybutyrate) (PHB), a homopolymer composed of 3-hydroxybutyrate (3HB, C4) units, and poly(3-hydroxyvalerate) (PHV), a homopolymer of 3-hydroxyvalerate (3HV, C5) units.[1][6] Copolymers such as poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV), which incorporate both 3HB and 3HV monomers in varying ratios, are also common and offer tunable properties based on composition.[1][18] The incorporation of monomers in scl-PHAs occurs through microbial metabolic processes. For PHB, two molecules of acetyl-CoA condense to form acetoacetyl-CoA, which is then reduced to (R)-3-hydroxybutyryl-CoA before polymerization.[19] PHV synthesis, in contrast, relies on propionyl-CoA as the key precursor, which can be derived from propionate or other odd-chain carbon sources and integrated into the polymer chain via similar enzymatic steps.[20] In PHBV copolymers, both acetyl-CoA and propionyl-CoA pathways contribute to the mixed monomer pool, allowing control over the 3HV content to adjust material characteristics.[21] Scl-PHAs exhibit high crystallinity, typically ranging from 50% to 90%, which contributes to their stiffness but can lead to brittleness.[22] PHB, for instance, has a melting point of approximately 175°C and a tensile strength of about 40 MPa, comparable to polypropylene.[23] These properties make scl-PHAs suitable for applications requiring thermal stability and rigidity, though the narrow gap between melting and decomposition temperatures poses processing challenges.[1] Primary producers of scl-PHAs are Gram-negative bacteria such as Cupriavidus necator (formerly Ralstonia eutropha), which can accumulate up to 80% of its dry cell weight as PHB under nutrient-limited conditions with excess carbon.[24][25] Other notable organisms include species from the genera Alcaligenes and Pseudomonas, though C. necator remains the most studied and efficient for industrial-scale PHB and PHBV production.[25][26]Medium-Chain-Length PHAs
Medium-chain-length polyhydroxyalkanoates (mcl-PHAs) are a subclass of bacterial polyesters characterized by repeating units of 3-hydroxyalkanoate monomers containing 6 to 14 carbon atoms (C6-C14), frequently occurring as copolymers with diverse monomer compositions.[27] Representative examples include homopolymers such as poly(3-hydroxyoctanoate) (PHO) and poly(3-hydroxydecanoate) (PHD), as well as copolymers like poly(3-hydroxyoctanoate-co-3-hydroxydecanoate) [P(3HO/3HD)].[28][29] The monomers are biosynthesized primarily through the β-oxidation pathway of fatty acids or de novo fatty acid synthesis, processes that often incorporate unsaturated or branched side chains into the polymer structure.[30][31] mcl-PHAs possess elastomeric qualities, including low crystallinity (typically 5-30%), glass transition temperatures typically ranging from -60°C to -30°C, and high elongation at break (up to 500%), which contribute to their flexible, rubber-like mechanical behavior.[32][33][34] These polymers are predominantly produced by Gram-negative bacteria of the genus Pseudomonas, with Pseudomonas putida serving as a key model organism due to its efficient accumulation of mcl-PHAs.[35]Biosynthesis
Natural Microbial Pathways
Polyhydroxyalkanoates (PHAs) are synthesized by a variety of bacteria through dedicated metabolic pathways that convert carbon sources into polymer granules stored intracellularly as carbon and energy reserves. These natural microbial pathways primarily involve the sequential action of enzymes that generate hydroxyacyl-coenzyme A (CoA) monomers, which are then polymerized into PHAs. The process is highly conserved across PHA-accumulating species, such as Cupriavidus necator, Pseudomonas spp., and Bacillus spp., and is activated under nutrient imbalance conditions to sequester excess carbon.[4] The key enzyme in PHA biosynthesis is PHA synthase (PhaC), a membrane-associated polymerase that catalyzes the final step of linking hydroxyacyl-CoA monomers into high-molecular-weight PHA chains via ester bond formation, releasing CoA. PhaC enzymes are classified into four classes (I–IV) based on their subunit composition, substrate specificity, and primary structure: Class I and II are typically homodimers or monomers (around 61–64 kDa), with Class I preferring short-chain-length (scl) monomers (C3–C5) and Class II favoring medium-chain-length (mcl) monomers (C6–C14); Classes III and IV are heterodimers consisting of a catalytic PhaC subunit (around 40 kDa) paired with PhaE or PhaR subunits, respectively, and generally incorporating scl monomers. This classification reflects evolutionary adaptations in different bacterial genera, such as Ralstonia for Class I and Pseudomonas for Class II.[36][37] The main biosynthetic routes diverge based on the carbon source and PHA type produced. For scl-PHAs like poly(3-hydroxybutyrate) (PHB), synthesized via the acetyl-CoA pathway (Type I), the process starts in central metabolism where two molecules of acetyl-CoA are condensed by β-ketothiolase (PhaA) to form acetoacetyl-CoA, which is then stereospecifically reduced by acetoacetyl-CoA reductase (PhaB, an NADPH-dependent enzyme) to (R)-3-hydroxybutyryl-CoA; this monomer is subsequently polymerized by PhaC. A simplified representation of the PHB pathway is:Genetic and Metabolic Engineering
Genetic and metabolic engineering has significantly advanced the production of polyhydroxyalkanoates (PHAs) by modifying microbial hosts to improve biosynthesis efficiency and expand monomer diversity. A primary strategy involves the overexpression of key PHA biosynthetic genes, such as phaA (encoding β-ketothiolase), phaB (acetoacetyl-CoA reductase), and phaC (PHA synthase), often sourced from natural producers like Ralstonia eutropha. In Escherichia coli, heterologous expression of the phaCAB operon from R. eutropha enables PHA accumulation, with engineered strains achieving up to 80% of cell dry weight (CDW) as poly(3-hydroxybutyrate) (PHB) under optimized conditions. Similarly, in yeast hosts like Saccharomyces cerevisiae, introduction of pha genes from bacterial sources allows PHA synthesis from lignocellulosic sugars, though yields typically range from 5-15% CDW due to compartmentalization challenges in eukaryotic cells.[44][45][46] Pathway engineering further enhances PHA yields by redirecting central carbon metabolism toward precursor accumulation and eliminating competing pathways. For instance, knocking out genes involved in glycolysis or the tricarboxylic acid cycle, such as ldhA (lactate dehydrogenase) and pflB (pyruvate formate-lyase) in E. coli, increases NADPH availability and carbon flux to PHA precursors, boosting PHB content to over 40% CDW. In Ralstonia eutropha (now Cupriavidus necator), metabolic modifications targeting the propionate assimilation pathway, including disruption of prpC genes, enable production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) copolymers directly from glucose, with 3-hydroxyvalerate (3HV) fractions up to 29 mol% and overall PHA accumulation reaching 69% CDW in fed-batch fermentations. Introducing PHA synthases from diverse bacteria, such as PhaC from Pseudomonas stutzeri into E. coli, facilitates incorporation of medium-chain-length monomers like 3-hydroxyoctanoate, yielding copolymers with tailored properties. Engineered strains utilizing inexpensive substrates like glycerol have demonstrated PHA contents up to 90% CDW, highlighting the scalability of these approaches.[45][47][48][49] Advanced tools like CRISPR-Cas9 have revolutionized precise gene editing for PHA engineering, enabling scarless deletions and insertions to optimize pathways. In C. necator, CRISPR-Cas9-mediated genome editing has been used to disrupt PHA depolymerase genes (phaZ), resulting in hyperaccumulation of PHB up to 85% CDW by preventing intracellular degradation. Synthetic biology approaches, including modular pathway assembly and reversed β-oxidation cycles, allow the incorporation of novel monomers such as 4-hydroxybutyrate or unsaturated hydroxyalkanoates, expanding PHA structural diversity beyond natural limitations. These techniques, applied in hosts like Pseudomonas putida, have yielded copolymers with up to 20% novel monomer content from renewable feedstocks.[50][51]Production
Laboratory-Scale Methods
Laboratory-scale production of polyhydroxyalkanoates (PHAs) primarily relies on controlled microbial fermentation in small-scale systems, such as shake flasks or benchtop bioreactors with working volumes of 1-10 L, enabling precise manipulation of environmental parameters to maximize PHA accumulation under nutrient limitation. These methods facilitate rapid experimentation and optimization for various PHA types, often using pure or mixed microbial cultures.[52] Fed-batch fermentation is the most widely adopted technique at this scale, involving an initial growth phase in batch mode followed by controlled, intermittent feeding of carbon sources to achieve high cell densities while avoiding substrate inhibition or catabolite repression. This strategy supports PHA contents of 20-80% of cell dry weight (CDW), with productivities typically ranging from 0.5 to 2 g/L/h depending on the strain and substrate.[53][54] Common substrates include pure carbohydrates like glucose or fructose, as well as low-cost alternatives such as waste oils (e.g., canola oil) or agro-industrial residues like banana peel hydrolysate, which promote tailored PHA copolymer synthesis. Nutrient limitation, particularly nitrogen or phosphorus restriction, is imposed during the feeding phase to redirect carbon flux toward PHA biosynthesis.[55][53] Post-fermentation, biomass is harvested via centrifugation, followed by extraction and purification. Chloroform is the standard solvent for laboratory extraction, where dried cells are incubated at 60°C to dissolve PHA, which is then precipitated with cold methanol or ethanol, achieving recoveries of 85-95%. Enzymatic digestion with proteases (e.g., proteinase K) or lysozyme offers a milder, eco-friendly alternative, selectively degrading non-PHA cell mass with yields up to 90%, though it requires longer incubation times (12-24 hours) at 37°C. Purification involves solvent evaporation under reduced pressure and repeated precipitation to remove impurities, ensuring polymer purity above 95%.[56][57] Analytical characterization employs nuclear magnetic resonance (NMR) spectroscopy to confirm monomer composition—for example, identifying 3-hydroxybutyrate (HB) and 3-hydroxyhexanoate (HHx) ratios in copolymers—and gel permeation chromatography (GPC) to determine molecular weight, with PHA samples typically exhibiting weight-average molecular weights (Mw) of 50,000-1,000,000 Da and polydispersity indices of 1.5-2.5.[58][59] Optimization focuses on maintaining pH at 6-7 via automated acid/base addition, temperature at 28-30°C for optimal enzyme activity, and aeration to sustain dissolved oxygen levels of 20-30% for aerobic strains, preventing oxygen limitation that could reduce yields by up to 40%. Safety considerations include sterile techniques to avoid contamination and proper handling of volatile solvents like chloroform in fume hoods. Engineered microbial strains, such as recombinant Escherichia coli expressing PHA synthase genes, can be integrated into these fed-batch setups to boost yields beyond native producers.[60][61][62]Industrial Processes
Industrial production of polyhydroxyalkanoates (PHAs) primarily relies on microbial fermentation processes scaled to commercial levels, utilizing large bioreactors ranging from 100 to 500 m³ in volume. These processes typically employ either batch or continuous fermentation modes, with mixed microbial cultures (MMCs) favored for their ability to utilize low-cost, renewable feedstocks and reduce the need for sterile conditions compared to pure culture systems.[62][63][64] Key substrates in industrial PHA manufacturing include agro-industrial wastes such as sugarcane molasses and industrial effluents, which lower production costs by repurposing waste streams, alongside plant-based oils like canola oil for specific PHA variants. For instance, Danimer Scientific produces its Nodax™ PHA through fermentation of canola oil using proprietary microorganisms in large-scale facilities.[65][66][62] Downstream processing begins with cell disruption to release intracellular PHA granules, followed by solvent-free extraction methods such as supercritical CO₂ to achieve high-purity polymers without residual solvents, and concludes with drying and pelletization for commercial use. These steps are optimized for efficiency and sustainability, minimizing energy inputs and environmental impact in full-scale operations.[67][68] As of 2025, global PHA production capacity is approximately 50,000 tons per year, with manufacturing costs ranging from $4 to $6 per kg, influenced by feedstock prices and process efficiencies. Leading producers include TianAn Biologic in China, which operates a 2,000-ton annual facility focused on poly(3-hydroxybutyrate) (PHB) and copolymers via fermentation, and RWDC Industries, which expanded its PHA plant in Athens, Georgia, USA, to support commercial-scale output starting in the early 2020s.[3][62][69][70]Properties
Physical and Mechanical Properties
Polyhydroxyalkanoates (PHAs) exhibit a range of physical and mechanical properties that make them viable alternatives to conventional petroleum-based plastics such as polypropylene and polyethylene, though their behaviors vary significantly by chain length and composition. Short-chain-length PHAs (scl-PHAs), like poly(3-hydroxybutyrate) (PHB), display thermoplastic characteristics with high crystallinity, while medium-chain-length PHAs (mcl-PHAs) are more elastomeric and amorphous. These properties are influenced by molecular weight, copolymerization, and processing conditions, enabling applications in molding and extrusion similar to synthetic polymers.[17]Thermal Properties
The thermal behavior of PHAs is characterized by their melting temperature (Tm), glass transition temperature (Tg), and decomposition temperature, which determine processability and stability during manufacturing. For scl-PHAs, such as PHB, the Tm typically ranges from 140°C to 180°C, with pure PHB exhibiting a Tm around 175–180°C, allowing melt processing without excessive degradation. In contrast, mcl-PHAs have lower Tm values, often between 40°C and 60°C, reflecting their softer, rubber-like nature. The Tg for scl-PHAs is relatively higher, around 0°C to 5°C for PHB, whereas mcl-PHAs show Tg values from -40°C to -30°C, contributing to flexibility at low temperatures. Thermal stability is generally good up to 250°C for most PHAs, with onset of decomposition occurring above 200–250°C under inert conditions, though exposure to oxygen can accelerate degradation. These parameters are commonly assessed using differential scanning calorimetry (DSC), which measures heat flow during phase transitions to quantify Tm and Tg precisely.[17]Mechanical Properties
Mechanically, PHAs span from rigid to flexible profiles depending on their type, with scl-PHAs being stiff and brittle, akin to polystyrene, while mcl-PHAs are tough and ductile, resembling elastomers. For PHB, the Young's modulus ranges from 0.5 GPa to 3.5 GPa, indicating high stiffness, with tensile strength around 30–40 MPa and elongation at break typically 3–8%, leading to brittle failure under strain. mcl-PHAs, however, exhibit much lower Young's modulus (0.005–0.1 GPa or 5–100 MPa) and tensile strength (10–20 MPa), but superior elongation at break of 200–500%, enabling high ductility and energy absorption. This contrast arises from the side-chain branching in mcl-PHAs, which reduces crystallinity and enhances toughness. Tensile properties are evaluated per ASTM D638 standards, involving standardized specimen testing to measure modulus, strength, and elongation under controlled conditions.[17]| Property | scl-PHAs (e.g., PHB) | mcl-PHAs |
|---|---|---|
| Young's Modulus | 0.5–3.5 GPa | 0.005–0.1 GPa |
| Tensile Strength | 30–40 MPa | 10–20 MPa |
| Elongation at Break | 3–8% | 200–500% |
| Behavior | Brittle, rigid | Ductile, flexible |