Industrial Production of PHA -
A subsidiary of ICI Ltd. in Great Britain produces Biopol from Alcaligenes eutrophus (H16). Either PHB homopolymer or copolymers of PHB and B-hydroxyvalerate can be produced by these cells depending on the substrate or substrate mixture used for growth and production. For industrial applications it is desirable to control the incorporation of different repeating units i nto the polymer in order to produce polyesters with specific material characteristics because their physical and chemical properties depend strongly on copolymer composition. Tailor-made copolymers can be made for this purpose by the use of controlled conditions. If a defined mixture of nutrients for certain type of microorganisms is supplied for growth, a defined and reproducible copolymer is formed. Biochemically there are 2 different ways of achieving polymer formation in microbes
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Parallel process has been demonstrated in R.rubrum and P.oleovorans. During cell growth, however part of the polymer forming potential is lost because of its utilization of substrate to maintain the cell's metabolism. In serial process of industrial polymer production micro-organisms are first grown on C source to obtain large biomass, then the medium is depleted of a n essential nutrient and polymer forming substrate is added. This is converted directly to polymers and essentially only little growth occurs. This approach is used for large scale PHA production by A. eutrophus.
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List of limiting components leading to PHA formation -
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Biopol of ICI is produced by using Alcaligenes eutrophus. Polymer separation and purification is accomplished by using a proprietary aqueous wash process followed by drying. PHB is too stiff and brittle for most applications, so the ICI add s a small amount of simple organic acid to the sugar feed stock to make the plastic stronger and more flexible. In technical terms, bacteria then produce co-polymers composed of PHB with varying amounts of hydroxyvalerate (HV). In this way ICI can produce a range of thermoplastic polymers which can be processed with conventional techniques to make bottles, mouldings, fibres and films. High grade Biopol is being made for medical applications, including woven patches for use inside the body to protect tissue s from scarring after surgery. After the wound is healed, enzymes in the blood dissolve away the patch. ICI's biodegradable plastic (thermoplastic Biopol) has found its North American applications as a blow-molded bottle and injection-molded caps for hair c are products. The Berlin Packaging corporation, Chicago will produce bottles and caps. Biopol currently sells for $ 8-10 per lb but is expected to sell for $ 4 per lb. The ICI company has currently a capacity of 600,000 lb per year in Billingham, UK. Annual production of 11 billion lbs is predicted by late 1990s. Biotehnologische Forschungsgesellschaft mbH in Austria produces PHB on a technical scale from cells of Alcaligenes latus with sucrose as a carbon source.
Biopol has been used in Germany since 1990 to make the bottles of Wella's Sanara Shampoo. Biopol's US launch came in 1995, in the form of bottles for Brocanto International's Evanesce shampoo and material is being tested in the UK for cosmetic containers.
Japan also has shown interest in Biopol. Biopol has been introduced there in 1991 as a container for Ishizawa Kenkyujo's Earthic Alga shampoos and conditioners. Now three more hair care companies of Japan have started using Biopol containers and shortly Kai will use it for disposable razor with B iopol handle. Rubbish bags, disposable nappies, paper plates, cups coated with thin plastic film can be made with Biopol and will get degraded when thrown in landfill. Biopol shampoo bottle disappears in two years in typical dung.
With development in yields, productivity, use of newer strains PHB concentration and productivity of 100 g.l-1 and 2.5 g.l-1 h-1 can be reached.
Chemi Linz AG began to develop a process for PHB production by fermentation in 1980s. Their polymer group Petrochemia Danubia (PCD) carries out the fermentation process through btF, a biotechnological research unit. The PCD process is different in that it uses Alcaligenes lactus as the producing organism and sucrose as the substrate. PHB formation is growth associated and nutrient limitation is not used to induce polymer accumulation. Solvent extraction is used to extract the product. It is a PHB homopolymer which is made. PCD-Polymere, an Austrian polyolefin producer developed a production process for PHB and processing technology for injection moulding and blow moulding. An Austrian biotechnology research company has developed a process for PCD-Polymere.
The fermentation process is based on a unique bacterial strain Alkaligenes latus. The strain is isolated from soil in California and Au stralia. It produces PHB in large amounts (80% of cell dry weight) during unlimited growth. Proprietary fermentation process developed is scaled upto 10 m3 of fermentation volume. In a fed batch mode more than 1 ton of PHB can be produced in less than a week. These fermentations are carried out in common stirred tank reactors, but other reactors like air lift or bubble column may also be used to get similar good results. The fermentation is carried out in mineral salts medium, sucrose or glucose as source of carbon. If precursors like propionic acid are added then co-polymers of PHB/HV can be produced as well as co-polymers of 3HB/4HB (3-hydroxybutyrate-co-4hydroxybutyrate) if 1,4 butanediol is added as precursor.
After fermentation cells are harvested, was hed with tap water and a concentrated suspension of 200 g/l is prepared. This suspension is directly used for the extraction process. The cell suspension is treated with solvent (methylene chloride). After this extraction step solvent is separated by cent r ifugation. The dissolved PHB is precipitated in water, recovered as white powder and dried. After one extraction step and one precipitation step PHB of 99% purity is obtained. This powder is directly used for compounding and further processing. Biomass can be recovered after the extraction process. It was tested as soil enhancer.
PCD-Polymere films and fibres are under development. Good results were obtained for injection moulding and blow moulding parts. PCD also helps others to develop further the technology.
The cost of producing PHB can be substantially reduced if methanol is used as substrate. Methanol is one of the cheapest noble substrates available, and has several advantages as fermentation substrate (purity, solubility, availability etc.) and is non-food substrate. Methanol can be easily obtained from natural gas and may also be obtained from biomass if necessary.
Methylobacterium extorquens is the isolate (gram negative, motile, pink pigmented bacterium can be used. Average PHB contents are found to be 25-30% of dry weight. It was also capable of producing PHV with the ratio of PHV to PHB of 0.2. Good process control was essential in the development of high cell-density fed-batch fermentation process for PHB production from methanol. Biomass leve l of 120 g/l and PHB levels of 60 g/l could be reached.
Evaluatiuon of different extraction and cell rupture methods for PHA isolation from Rhodospirillum rubrum -
| Hot Chloroform Extraction | Lysozyme Sonication | French Press | Hypochlorite | |
| PHA content (% dry weight) | 13.6 | 13.6 | 13.6 | 13.6 |
| Isolated PHA (% dry weight) | 12.5 | 9.7 | 7.7 | 12.1 |
| Recovery % | 92 | 71 | 58 | 89 |
| Mw (x 10-6) | 1.5 | 0.92 | 0.65 | 0.94 |
| Mn (x 10-6) | 1.1 | 0.36 | 0.46 | 0.37 |
| Mw / Mn (Polydispersity) | 1.4 | 2.6 | 1.4 | 2.5 |
Market for Biodegradable Material -
During the early 1990s, annual production of PHAs was just several hundred tonnes. In 1996 Zeneca, the main producer has stopped producing PHBV and sold the assets to Monsanto and Astra. Currently, the market for biodegradable material is largest in Scandi navia and other European countries, where companies are willing to pay up to pounds 4 per kg for PHAs. The estimate given in table below is based on the development of a composting infrastructure, which is now becoming highly developed in many parts of Eu rope, particularly in Germany, Holland and Belgium.
Western European market estimates for biodegradable plastics (tonnes per annum) -
| Applications | Conventional Resins | Biodegradable Resins |
| Waste Disposal Bags for Composting | - | 30 000 |
| Disposable Fast Food Utensils | 100 000 | 50 000 |
| Hygiene Films | 110 000 | 20 000 |
| Paper Coatings | 420 000 | 40 000 |
| Agricultural Sector | 65 000 | 30 000 |
| Total | 695 000 | 170 000 |
| Source - BASF |