| Literature DB >> 31405025 |
Justyna Możejko-Ciesielska1, Paulina Marciniak2, Karolina Szacherska2.
Abstract
The negative effects of petrochemical-derived plastics on the global environment and depletion of global fossil fuel supplies have paved the way for exploring new technologies for the production of bioplastics. Polyhydroxyalkanoates (PHAs) are considered an alternative for synthetic polymers because of their biodegradability, biocompatibility, and non-toxicity. Many bacteria have been reported to have the ability to synthesize PHAs. Among them, the Aeromonas species seem to be ideal hosts for the industrial production of these biopolyesters due to their robust growth, simple growth requirements, their ability for the synthesis of homopolymers, co-polymers, and terpolymers with unique material properties. Some Aeromonas strains were able to produce PHAs in satisfactory amounts from simple carbon sources. Efforts have been made to use genetically modified Aeromonas strains for enhanced PHAs and to obtain bacteria with modified compositions and improved properties. This review discusses the current state of knowledge of polyhydroxyalkanoates synthesized by Aeromonas species, with a special focus on their potential, challenges, and progress in PHA synthesis.Entities:
Keywords: Aeromonas spp.; biodegradable polymers; biopolymers; polyhydroxyalkanoates
Year: 2019 PMID: 31405025 PMCID: PMC6722653 DOI: 10.3390/polym11081328
Source DB: PubMed Journal: Polymers (Basel) ISSN: 2073-4360 Impact factor: 4.329
Figure 1Chemical formulae of polyhydroxyalkanaotes (PHAs). (A) P(3HB); (B) P(3HO), (C) P(3HB-co-3HHx) [4].
Figure 2Metabolic pathways for synthesis of PHAs by the Aeromonas species.
An overview of microbial synthesis of PHAs by Aeromonas sp. grown on different carbon sources.
| Bacteria | Substrate | Environmental Stress | Biomass Concentration (g/L) | PHA Content (%) | Type of PHAs | References |
|---|---|---|---|---|---|---|
|
| glucose | without limitation | 3.25 | nd | nd | [ |
| P-limitation | 1.90 | 15.6 | P(3HB) | |||
| N-limitation | 0.55 | nd | nd | |||
| sodium gluconate | without limitation | 3.05 | nd | nd | ||
| P-limitation | 4.63 | 35.1 | P(3HB) | |||
| N-limitation | 0.58 | nd | nd | |||
| lauric acid | without limitation | 7.68 | 19.5 | P(3HB-co-HHx) | ||
| P-limitation | 2.83 | 28.8 | P(3HB-co-HHx) | |||
| N-limitation | 1.70 | 22.5 | P(3HB-co-HHx) | |||
| lauric acid and glucose | N-limitation | 11.20 | 22.0 | P(3HB-co-HHx) | [ | |
| P-limitation | 16.20 | 51.5 | P(3HB-co-HHx) | |||
| dodecanoic acid | N-limitation | 3.50 | 58.9 | P(3HB-co-HHx) | [ | |
| lauric acid | N-limitation | 2.24 | 49.0 | P(3HB-co-HHx) | [ | |
| oleic acid | 0.52 | 43.0 | P(3HB-co-HHx) | |||
| dodecanoic acid | without limitation | 40.4 | 54.6 | P(3HB-co-HHx) | [ | |
| dodecanoic acid + gluconate | 12.00 | 32.0 | P(3HB-co-HHx) | |||
| starch | N-limitation | 1.74 | 1.8 | P(3HB-co-HHx) | [ | |
| lauric acid | 1.32 | 68.2 | P(3HB-co-HHx) | |||
| undecanoic acid | N-limitation | 5.01 | 45.2 | P(3HV) | [ | |
| lauric acid and valeric acid | N-limitation | 3.56 | 19.6 | P(3HB-co-3HV-3HHx) | [ | |
| lauric acid and valeric acid | 1.18 | 41.4 | P(3HB-co-3HV-3HHx) | |||
| lauric acid and valeric acid | 1.15 | 35.1 | P(3HB-co-3HV-3HHx) | |||
| lauric acid | N-limitation | 4.85 | 40.7 | P(3HB-co-HHx) | [ | |
| hexanoate | 0.61 | 8.8 | P(3HB-co-HHx) | |||
| octanoate | 1.18 | 13.5 | P(3HB-co-HHx) | |||
| lauric acid | N-limitation | 4.15 | 50.7 | P(3HB-co-HHx) | [ | |
| dodecanoate | N-limitation | 4.73 | 49.7 | P(3HB-co-HHx) | [ | |
| dodecanoate | N-limitation | 2.43 | 11.2 | P(3HB) | ||
|
| coconut oil | N-limitation | 7.31 | 49.6 | P(3HB) | [ |
| pure glycerol | N-limitation | 2.53 | 4.7 | P(3HB) | [ | |
| P-limitation | 2.32 | 42.0 | P(3HB) | |||
| crude glycerol | N-limitation | 2.00 | 2.8 | P(3HB) | ||
| P-limitation | 2.65 | 13.6 | P(3HB) |
3HB—3-hydroxybutyrate; 3HV—3-hydroxyvalerate; 3HHx—3-hydroxyhexanoate; N-limitation—nitrogen limitation; P-limitation—phosphorus limitation; nd—not detected.
PHAs production by genetically modified Aeromonas spp.
| Genetically Modified Bacteria | Gene Donor | Carbon Source | Biomass Concentration (g/L) | PHA Content (%) | Type of PHAs | References |
|---|---|---|---|---|---|---|
|
| dodecanoate | 3.7 | 51.6 | P(3HB-co-3HHx) | [ | |
| 4.4 | 57.8 | P(3HB-co-3HHx | ||||
| 4.3 | 58.9 | P(3HB-co-3HHx) | ||||
| lauric acid | 3.2 | 47.3 | P(3HB-co-3HHx) | [ | ||
| gluconate | 6.9 | 13.7 | P(3HB-co-3HHx) | [ | ||
|
| dodecanoate | 51.5 | 62.0 | P(3HB-co-3HHx) | [ | |
| dodecanoate + sodium gluconate | 32.8 | 52.0 | P(3HB-co-3HHx) | |||
| lauric acid | 4.9 | 49.9 | P(3HB-co-3HHx) | [ | ||
| lauric acid | 5.1 | 53.4 | P(3HB-co-3HHx) | |||
|
|
| dodecanoate + gluconate | 2.5 | 2.9 | P(3HHx-co-3HO-co-3HD-co-3HDD) | [ |
|
| dodecanoate + gluconate | 3.6 | 20.9 | P(3HB-co-3HHx-co-3HO-co-3HD-co-3HDD) | ||
|
| dodecanoate + propionate | 3.3 | 35.6 | P(3HB-co-3HV-co-3HHx) | [ | |
| glucose | 1.3 | 36.8 | P(3HB-co-3HHx) | [ | ||
| starch | 1.8 | 32.7 | P(3HB-co-3HHx) | |||
| lauric acid | 1.6 | 59.4 | P(3HB-co-3HHx) | |||
|
| lauric acid | 4.8 | 58.6 | P(3HB-co-3HHx) | [ | |
| lauric acid + | 4.0 | 24.2 | P(3HB-co-4HB-co-3HHx) | |||
|
| undecanoate | 5.6 | 47.7 | P(3HV) | [ | |
|
| valerate 0.5 g/L | 3.7 | 45.4 | P(3HB-co-3HV-co-3HHx) | [ | |
| valerate 1 g/L | 4.7 | 59.3 | P(3HB-co-3HV-co-3HHx) | |||
| valerate 2 g/L | 2.4 | 71.1 | P(3HB-co-3HV-co-3HHx) | |||
|
| sodium hexanoate | 3.0 | 54.5 | P(3HB-co-3HHx) | [ | |
| sodium octanoate | 3.1 | 50.6 | P(3HB-co-3HHx-co-3HO) |
3HB—3-hydroxybutyrate; 4HB—4-hydroxybutyrate; 3HV—3-hydroxyvalerate; 3HHx—3-hydroxyhexanoate; 3HO—3-hydroxyoctanoate.
Comparison of material properties of PHAs extracted from Aeromonas sp. cells and synthetic polymers.
| Bacteria | Type of PHAs/Synthetic Polymers | Molecular Weight ( | Young’s Modulus (MPa) | Elongation to Break (%) | Tensile Strength (Mpa) | Biodegradation | References | |||
|---|---|---|---|---|---|---|---|---|---|---|
| Recombinant | P(84.7% 3HB-co-5.4% 3HV-co-9.9% 3HHx | 37.3 | −2.6 | 273.1 | 129 | nd | nd | nd | high rate | [ |
| P(83.7% 3HB-co-1.2% 3HV-co-15.1% 3HHx) | 52.8 | −1.8 | 248.5 | 104 | nd | nd | nd | |||
| P(88.3% 3HB-co-1.0% 3HV-co-10.7% 3HHx) | nd | nd | nd | nd | 318.9 | 276.9 | 10.1 | |||
| P(84.2% 3HB-co-2.4% 3HV-co-13.4% 3HHx) | nd | nd | nd | nd | 109.8 | 481.1 | 8.0 | |||
| Recombinant | P(73.7% 3HB-co- 4.3% 4HB-co- 22% 3HHx) | 66.6 | −9.3 | 253 | nd | 3.8 | 504 | 0.6 | high rate | [ |
| P(73.8% 3HB-co-7.6% 4HB-co-18.6% 3HHx) | 75.4 | −11.7 | 245 | nd | 2.85 | 143 | 0.3 | |||
| Recombinant | P(3HV) | 23.0 | −15.8 | 258 | 103 | nd | nd | nd | high rate | [ |
| Recombinant | P(75.3% 3HB-co-13.1% 3HV-co-11.7% 3HHx) | 94.4 | −1.8 | 248.1 | 101.3 | nd | nd | nd | high rate | [ |
| P(47.9% 3HB-co-23.8% 3HV-co-28.3% 3HHx) | 94.2 | −5.1 | 250.5 | 54.2 | nd | nd | nd | |||
| P(78.8% 3HB-co-10.9% 3HV-co-10.3% 3HHx) | nd | nd | nd | nd | 234.9 | 340.9 | 8.4 | |||
| P(55.2% 3HB-co-25.7% 3HV-co-19.1% 3HHx) | nd | nd | nd | nd | 2.08 | 133.3 | 0.3 | |||
| Recombinant | P(4% 3HB-co-96% 3HHx) | 30.0 | −20.8 | 257 | nd | nd | nd | nd | high rate | [ |
| P(3% 3HB-co-87% 3HHx-co-10% 3HO) | 16.0 | −23.2 | 264 | nd | nd | nd | nd | |||
|
| ||||||||||
| Polypropylene | nd | −10 | nd | 176 | 1.7 | 400 | 34.5 | slow rate | [ | |
| Polystyrene | nd | 100 | nd | 240 | 3.1 | nd | 50 | |||
| Polyethylene | nd | −30 | nd | 130 | 0.2 | 620 | 10 | [ | ||
3HB—3-hydroxybutyrate; 4HB—4-hydroxybutyrate; 3HV—3-hydroxyvalerate; 3HHx—3-hydroxyhexanoate; 3HO—3-hydroxyoctanoate; Mw—weight-average molecular weight; Tg—glass-transition temperature; Tm—melting temperature; Td—Temperature at 5% weight loss was determined by TGA; nd—not detected.
Figure 3Advantages of using Aeromonas spp. for large scale production of polyhydroxyalkanoates.