AU601681B2 - Creación de Inventos y Patentes con Inteligencia Artificial

AU601681B2 – Poly beta-hydroxybutyric acid/poly beta-hydroxyvaleric acid copolymer production
– Google Patents

AU601681B2 – Poly beta-hydroxybutyric acid/poly beta-hydroxyvaleric acid copolymer production
– Google Patents
Poly beta-hydroxybutyric acid/poly beta-hydroxyvaleric acid copolymer production

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Publication number
AU601681B2

AU601681B2
AU57825/86A
AU5782586A
AU601681B2
AU 601681 B2
AU601681 B2
AU 601681B2
AU 57825/86 A
AU57825/86 A
AU 57825/86A
AU 5782586 A
AU5782586 A
AU 5782586A
AU 601681 B2
AU601681 B2
AU 601681B2
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AU
Australia
Prior art keywords
substrate
alcohol
copolymer
carbon
alcaligenes eutrophus
Prior art date
1985-05-28
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AU57825/86A
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AU5782586A
(en

Inventor
Stephen Hugh Collins
Kenneth Raymond Richardson
Peter James Senior
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Monsanto Co

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Imperial Chemical Industries Ltd
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1985-05-28
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1986-05-22
Publication date
1990-09-20

1986-05-22
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Imperial Chemical Industries Ltd

1986-12-04
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1990-09-20
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1990-09-20
Publication of AU601681B2
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1994-06-23
Assigned to ZENECA LIMITED
reassignment
ZENECA LIMITED
Alteration of Name(s) in Register under S187
Assignors: IMPERIAL CHEMICAL INDUSTRIES PLC

1998-02-19
Assigned to MONSANTO COMPANY
reassignment
MONSANTO COMPANY
Alteration of Name(s) in Register under S187
Assignors: ZENECA LIMITED

2006-05-22
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Classifications

C—CHEMISTRY; METALLURGY

C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON

C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS

C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule

C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds

C08G63/06—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids

C—CHEMISTRY; METALLURGY

C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING

C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE

C12P7/00—Preparation of oxygen-containing organic compounds

C12P7/62—Carboxylic acid esters

C12P7/625—Polyesters of hydroxy carboxylic acids

Abstract

Copolymers of poly( beta -hydroxybutyric acid) and poly( beta -hydroxyvaleric acid) are produced by culturing alcohol-utilising strains of Alcaligenes eutrophus on a carbon source including primary alcohols having an odd number of carbon atoms such as propan-1-ol.

Description

01I
AUSTRALIA
Patents Act 00 0 416 8 1 It COMPLETE SPECIFICATION
(ORIGINAL)
Class Int. Class Application Number:- Lodged: Complete Specification Lodged: Accepted: Published: Priority Related Art: I ElmnciL~;;L Z ‘for prnt»~ iU~b~c
H
7~ Naine(s) of Applicant(s): Address(es) of Applicant(s).* t AictuaI Inventor(s): Address for Service is: APPLICANT’S REF.; 13. 335041IAU IMPERIAL CHEMICAL INDUSTRIES PLC Imperial Chemical House, Milibank, London SWIP 3JFo
ENGLAND.
Peter James SENIOR Stephen, Hugh COLLINS Kenneth RaYmond RICHARDSON PHILLIPS, ORMONDZ AND FITZPATRICK Patent and Trade. Mark Attorneys 367 Collins Street Melbourne, Australia, 3000 invention entitled: F3 P~Re E! I E)N Complete Specification for the Iowing statement is a full description of this invention, Including the best methiod of performing, it known to ic l 1 a B 33504 P I- -rO b c potY P AroyVo&\e ‘%IC c.c-,\r Copolymer produration *opoln^ fr The present invention relates to a process of producing copolymers and in particular to a process of producing copolymers of P-hydroxybutyric acid and jit +ke c iFPt+id0 -rv cnr-shydroxyvaleric acids. Hereinafter poly f-hydroxybutyric acid is referred to as PHB and poly B-hydroxyvaleric acid is referred to as PHV. Thus the present invention relates to the production of PHB/PHV copolymers.
PHB is a thermoplastic polyester comprising repeat units of the formula:
-CH(CH
3
)CH
2
COO-
which is accumulated by many micro-organisms, particularly S4 bacteria, for example of the genera Alcaligenes, Athiorhodium, Azotobacter, Bacillus, Nocardia, Pseudomonas, 15 Rhizobium and Spirillium, as an energy reserve material.
o 1 Poly 3-hydroxybutyric acid is conveniently prepared by cultivating the micro-organism in an aqueous medium on a suitable substrate, such as a carbohydrate or methanol, as an energy and carbon source. The substrate must, of course, be a «4 20 one that is assimilable by the micro-organism. In order to promote accumulation of the polymer, at least part of the i cultivation is preferably conducted under conditions wherein li there is a limitation of a nutrient that is essential for growth of the micro-organism but which is not required for polymer accumulation. Examples of suitable processes are described in EP-A-15669 and 46344 and USP 4$36334 and 4433053.
United States Patent 4477654 discloses that PHB/PHV copolymers can be made by cultivating certain microorganisms such as Alcaligenes eutrophus using certain organic acids, for example propionic acid, or derivatives thereof such as salts or esters, as at least part of the substrate during at least part of the polymer accumulating stage of the cultivation.
PHB/PHV copolymers have a variety of uses in many p i R .ii B j ¢t 4.
I f 4 94 4 19 9 9 «t t t f* 99 4 9 99 9* 9 4 I t 44 t 4 LIt 2 B 33504 fields of industry, for example see the article in Chemical Week, 28 August 1985, page 55 and in Manufacturing Chemist, October 1985, page 64.
Alcaligenes eutrophus does not normally utilise alcohols such as ethanol, see «The Prokaryotes» Chapter 70, p 882, ed M P Starr et al, published by Springer Verlag (1981).
However by mutation and/or selection procedures it is possible to obtain ethanol utilising mutants or variants.
We have found that such ethanol utilising variants are also capable of assimilating other primary alcohols, e.g.
propan-l-ol and, when cultivated on a substrate containing a primary alcohol having an odd number of carbon atoms, other than methanol, under conditions conducive to polymer accumulation, accumulate PHB/PHV copolymers.
15 Accordingly the present invention provides a process for producing a PHB/PHV copolymer comprising cultivating an alcohol-utilising Alcaligenes eutrophus strain, that is capable of accumulating poly(f-hydroxybutyrate), under such conditions that the micro-organism 20 accumulates at least 10% by weight of copolymer, wherein, for at l!dst part of the time when the micro-organism is cultivated under the copolymer-accumulating conditions, the subst’.te comprises at least one primary alcohol, other than mithanol, having an odd number of carbon atoms.
25 Alcohol utilising strains of Alcaligenes eutrophus that can be used include the strain CBS 388.76 whose production is disclosed in USF 4138291 and strain NCIB 12080 which was deposited with thei National Collection of Industrial Bacteria, Aberdeen on 2 May 1985. The latter strain can be obtained from a glucose-utilising strain for example NCIB 11599 (deposited with the National Collection of Industrial Bacteria on 18 August 1980) that does not utilise ethanol, by cultivating the strain, fo; example NCIB 11599, in continuous culture under oxygen limita&iori on glucose as substrate and then, transferring to carbon limitation on a substrate containing a
L~.
7″ ft ft.
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C
Ct ~t Iv C I Ct 3 B 33504 mixture of glucose and ethanol with progressive increase in the proportion of ethanol, relative to glucose, in the substrate until the substrate was wholly ethanol.
In general ethanol-utilising strains Alcaligenes eutrophus are obtained by inducing the enzyme ethanol dehydrogenase. This is conveniently performed by limitation of the oxygen supply. Once the enzyme is induced exposure to ethanol in a continuous culture results in selection of an ethanol-utilising strain. The oxygen availability can be 10 gradually increased to facilitate this selection.
When Alcaligenes eutrophus is aerobically cultured on a suitable substrate, i.e. a source of energy and carbon, reproduction occurs until one or more of the essential requirements for reproduction is exhausted. This 15 reproduction of the micro-organism is hereinafter referred to as growth. Upon exhaustion of an essential growth requirement, further growth occurs only to a very limited extent, if at all, but, providing the substrate is not exhausted, a P-hydroxybutyrate polymer may be accumulated by 20 the micro-organism.
With some micro-organisms, even in the absence of a polymer inducing constraint such as a lMiitation on one or more of the essential growth requirements, polymer may also be accumulated while growth of the micro-organism is taking 25 place: however, except in the case of micro-organisms that produce polymer constitutively, the amount of polymer so accumulated is generally small and typically is less than about 10% by weight of the cells produced. Although there can be a rise of polymer accumulation to about 30% by weight just before complete exhaustion. Thus when grown in batch culture, the micro-organisms that do not produce polymer constitutively, will grow, with little or no polymer accumulation, until one or more of the essential requirements for growth becomes nearly exhausted or exhausted, and then the micro-organism synthesises polymer. In order to produce 4 B 33504 copolymers it is necessary to use the alcohol containing an odd number of carbon atoms as at least part of the substrate present during the period when copolymer is accumulated.
When the cultivation conditions are such that copolymer is not being accumulated to any significant extent, i.e. where the conditions are such that the amount of copolymer accumulated is less than 10% by weight of the micro-organism cell dry weight, the odd numbered carbon atom alcohol will often be metabolised by the micro-organism by alternative pathways that do not give rise to copolymer: consequently in jf asuch cases copolymers will generally not be produced.
Metabolism by such other pathways may also occur when using micro-organisms that accumulate copolymer constitutively.
Hence we prefer, even, when using cotstitutive polymer-accumulating micro-organisms, to cause the copolymer j to be accumulated by cultivation of the micro-organism under conditions wherein the amount of one or more of the essential requirements for growth, but not polymer accumulation, is limited. Even when cultivating the micro-organism under conditions where there is a restriction of an essential requirement for growth, so that copolymer is accumulated by the micro-organism, some of the alcohol having an odd number of carbon atoms may be metabolised by pathways leading to acetyl CoA or intermediates of the TCA cycle. This enables the micro-organism to synthesise r-hydroxybutyrate units for incorporation into the copolymer as well as tthe g-hydroxyvalerate units, even if the alcohol containing the odd number of carbon atoms is the sole substrate during the polymer accumulation stage.
In order to produce copolymers, the substrate, during at least part of the period copolymer is being accumulated, contains a primary alcohol, other than methanol, containing an odd number of carbon atoms. The alcohol is preferably heptan-l-ol, pentan-l-ol, or particularly, propan-i-ol. Mixtires of such alcohols may be employed. The B 33504 alcohol, or alcohols, having an odd number oll carbon atoms may be used in admixture with another substrate assimilable by the micro-organism for example ethanol or a carbohydrate such as glucose.
In order to obtain a significant proportion of hydroxyvalerate units in the copolymer it is preferred that the amount of combined carbon in the substrate as the alcohol or alcohols having an odd number of carbon atoms is at least preferably at least 10%, by weight of the total combined carbon in the substrate present during the period when the cultivation conditions are such that copolymer is being VQ 0 accumulated by the micro-organism, Preferably the alcohol of alcohols having an odd number of carbon atoms form at least by weight of the substrate employed during the copolymer too. 15 accumulation stage.
.40 As indicated above, it is preferred, even when s o 0 using a micro-organism that produces copolymer constitutively, to conduct the period of cultivation of the 444* micro-organism when copolymer is being accumulated under a020 conditions of limitation of a nutrient required for growth but not for copolymer accumulation.
In addition to the substrate and oxygen (which is generally supplied by injecting air into the aqueous medium in the fermenter), various nutrient salts are required to 0 25 enable the micro-organism to grow. Thus sources of the following elements in assimilable form, normally as water soluble salts, are generally required: nitrogen, phosphorus, sulphur, potassium, sodium, magnesium, calcium, and iron, together with traces of elements such as manganese, zinc and i30 copper. While it may be possible to induce copolymer accumulation by restricting the supply of oxygen to the fermenter, it is preferred to restrict the amount of one or more of the nutrient salts. The most practical elements to limit are nitrogeaA phosphorus, oxygen, or, less preferably, magnesium, sulphur or potassium. Of thesv it is most 6 B 33504 preferred to restrict the amount of nitrogen (which is conveniently supplied as an ammonium salt). The amount of assimilable nitrogen required is about 8 15% by weight of the denired weight of cells less accumulated copolymer.
The fermentation is preferably conducted so that the dry weight of the copolymer-containing cells is at least g per litre of aqueous medium. Hence if, for example, it is desired to produce 10 g per litre of polymer-containing cells having a copolymer content of 40% by weight, the amount of the essential nutrient fed to the fermenter that is used S to limit the amount of cell growth must be that required to support the growth of 6 g per litre of cells containing no Scopolymer: thus, if nitrogen is employed as the growth Slimiting nutrient, since the nitrogen content of copolymer 1, 5 free bacterial cells is about 8 15% by weight, the amount of adsimilable nitrogen required would be between about and 0.9 g per litre, e.g. about 0.6 to 1.2 g of ammonium ions per litre.
0 The fermentation may be conducted under the conditions e.g. pH, temperature, and degree of aeration (unless oxygen is utilised as the limiting nutrient) conventionally used for Alcaligenes eutrophus micro-organisms.
Likewise the amounts of nutrient salts (other than the growth limiting mttrient whose amount may be determined following the considerations outlined hereinbefore) employed may be those normally used for growth of the micro-organism.
The micro-organism is preferably grown to a certain desired weight by cultivation in the presence of sufficient of the nutrient required for growth that is to be restricted in the copolymer accumulation stage on a rcadily metabolisable substrate, such as a carbohydrate, and then cultivated under conditions of growth requirement restriction to cause the copolymer accumulation. In some cases the substrate for at least part, and in some cases all, of the growth stage may be the alcohol having an odd number of O TO I qNM ‘l 9 1 a~I~ i-i r~L-n=nn~ 7 B 33504 carbon atoms.
The fermentation may be performed as a batch fermentation in which case copolymer accumulation will occur as the amount of the nutrient that is required for growth but not for copolymer accumulation becomes depleted. Alternatively the fermentation may be conducted as a continuous process wherein aqueous medium containing the bacterial cells is removed, continuously or intermittently, from the fermentation vessel at a rate corresponding to the rate of addition of fresh aqueous medium and substrate the’..vto. It is pr.ferred that the amount of the nutrient that is restricted that is fed to the fermentation vessel is such that the aqueous medium removed from the veasel contains little or none of that nutrient, aid the aqueous medium removed from the vessel is then fed to a second fermentation vessel, operated either in batch or, preferably, continuous fashion wherein copolymer accumulation is caused to take place by continuing the aerobic cultivation with the addition of a fresh quantity of substrate comprising the comonomer component. While additional quantities of substrate and nutrient salts may be added in this further fermentation step, since farther growth is generally not desired, little or no further quantity of the nutrient utilised to limit growth should be added. It will !owever be appreciated that the aqueous medium fed to the further fermenter or fermenters from the first fermenter may contain some residual quantity of the limiting nutrient and/or the addition of a further small quantity thereof may be desireable for efficient operation.
Alternatively the fermentation may be conducted as a single stage continuous process. In order to achieve copolymer accumulation by means of nutrient limitation the residence time of the medium in the fermenter is made sufficiently long to allow the micro-organism to grow and exhaust the limiting nutrient supplied to the fermenter and to allow the microorganism then to accumulate the copolyr~r.
I
IF
8 B 33504 In either a batch process, or continuous processes as described above, the alcohol having an odd number of carbon atoms is used as part, or all, of the substrate dutl-nR the copolymer accumulation stage occurring upon exiiaustion of the nutrient required for growth4 Tlvs fermentation is preferably conducted so that the amount of accumulated copolymer comprises about 30 to 80% by weight of the bacterial cells.
The copolymer, which generally has a molecular weight above 50,000 (weight average) and has the configuration, may be extracted from the micro-organism cells by a variety of techniques, for example those described in EP-A-15123.
The invention is illustrated by the following examples.
Description, of Alcaligenes eutrophus NOIB 12080 Grwhon CXiH0 75% agar, 5 hours at 30 0
C.
Gram negative motile rods of approximate size 0.8 pm x 6 pm.
Evidence of intra cellular granules.
No spore formatioti.
Under a phase contrast microscope occasional subpolar flagella were noted.
Colonial morphology (Lab 8 Nutrient Agar) the organiam is in the form of round, regular, opaque, smooth, white, convex colonies. After 3 days the diameter was about 2 mmi.
A pale brown pigmentation developed with increasing age4 Temperature At 5 0 C no growth.
At 37 0 C growth.
At 450C growth.
A
U I
C
I
1* 9 Gram staining (30 0
C)
Catalase Kovacs Oxidase 0-F glucose, very weakly oxidative Pyocyanin- Fluorescence L-Arginine CSU Betaine CSU Glucose CSU Lactate CSU Acetate CSU CSU arabinose Meso-itiositol xylose gas glucose ONPG Arginine Moller Lysine Moiler Ornith~ne Moller N0 3 to N0 2 NO, to N 2 at 3700 DNA ase Gel stab. Gel plate 25 Casein Starch Lecithin egg Lipase egg
NH
3 weakly positive Indole Tween 80 Urease No growth exh,,,bited on methanol at 5 or 14 days.
Growth exhibited on propan-l-oi at 3 days.
B33504 g a- Resistant to penicillin G and streptomycin; sensitive to chioramphenicol, tetracycline, polymyxin B and novobiocin (weakly).
Tho invention is further illustrated by the following examples in which Alcalicienes eutrophus is cultivated under nitrogen limiting conditions as here inbefore described.
be i-‘ Cc 4 1 1 4 A B 33504 4 4 0-l~~ -ehlormphonicol. tetracclina, pol;tmtxin E arn nrovob»i o (wPankly), EXAMPLE 1 Alcaligenes eutrophus variant NCIB 12080 was grown by continuous aerobic cultivation at pH 6.8 and 34 0 C in a 5 litre fetmenter with a working volume of about 4 litres at a dilution rate (reciprcc,! of residence time) of 0.1 hr The aqueous medium employed had the following composition, per litre of deionised water: mg Phosphorus (as H 3 P0 4 630 Magnesium (as MgSO 4 .7H 2 0) Potassium (as K 2
SO
4 200 Sodium (as Na 2 S04) 16 Manganese (as MnSO 4 .4H 3 0) 1.25 Zinc (as ZnSO 4 .7H 2 0) 1.15 Copper (as CuSO 4 .5H 2 0) 0.25 Calcium (as CaCO 2 .2H 2 0) 36 Iron and nitaogen were also continuously supplied, as aqueous solutions coAtaining 11.5 g/l of nitrogen as ammonium hydroxide and 2 g/l ferrous sulphate heptahydrate acidified with sulphuric acid respectively, at such rates that the nitrogen and iron contents of the medium fed to the fermenter 25 were 1040 mg/1 and 7 mg/l respectively.
Ethanol and propan-l-ol were supplied at a rate of 12.1 and 12.6 g/l respectively.
pH was controlled at 6.8’by the automatic addition of a 9:1 v/v mixture of 4 M potessium hydroxide and 4 M sodium hydroxide.
After 5 days steady state fermentation the cell dry weight of the effluent from the fermenter was 16.14 g.l and the cells contained 47% by weight of an PHB/PHV copolymer containing about 20 mol PHV units and having a melting point of 133 0 C (as determined by differential scan-ing calorimetry).
r I 1 O2i a _i i: 11. B 33504 EXAMPLE 2 Example 1 was repeated with the following changes: dilution rate 0.105 hr 1 Nitrogen concentration 976 mg/1 Propanol feed rate 21.4 g/1 Ethanol feed rate 0 After 5 days continuous steady state fermentation the cell dry weight was 12.02 g/l and the cells contained 38% by weight of a polymeric product. The polymeric product contained a higher overall PHV content than the polymer of Example 1 but was a complex product, exhibiting three distinct melting point peaks at 92.4°C, 110°C and 171°C. This is probably indicative that the polymer is a blend of a P-hydroxybutyrate homopolymer and one or more PHB/PHV copolymers.
EXAMPLE 3 Alcaligenes eutrophus NCIB 12080 wes grown in a fedbatch technique under aerobic cultivation cenditions at pH 6.8 ai;d 34°C in a 5 litre fermenter. NCIB 12080 culture (80 ml) was inoculated into aqueous medium (3.4 1) of the following composition, per litre of de-ionised water: mg Phosphorus (as H 3 P0 4 100 Potassium (as K 2 S0 4 250 Magnesium (MgSO 4 .7H 2 0) 250 S 25 Sodium (as Na 2
SO
4 Ammonium sulphate ((NH 4 2 S0 4 2000 Trace element soution: Calcium Manganese 1.25 Zinc 1.15 Copper 0.25 Iron 3 Ethanol 1800 The ph was controlled at 6.8 by the automatic addition of 0% vol/vol ammonium hydroxide solution.
12 B 33504 After 10.5 hours the ualture became carbon limited and a premixed feed of ethanol (335 gl~ and propan-l-ol (52 gl was introduced to the fermenter. Overall 620 mis of mixed feed was added to the farmenter over 33 hours so that there was an a’.erage rate of addition of ethanol of 2 gl hr hr
T
i- 2 The final cell dry weight was 33 gl-1 and the cells contained 71% by weight of PHB/PHV polymer containing about mol hydroxyvalerate units. This had a melting point of 1580C 10 as determined by differential scanning calorimetry.
4 49 *i 4 4:O( 09 4 4 94~ 4 44 8 44 f.
bi* 0 9$ 4 49 4 4494 9, 9 44 4 I 99
PA/PMD/MP
24 April 1986/LI$3

Claims (6)

1. A process for producing a 1 copolymer neA hd bt and polyhydroxyvalerate comprising cultivating a microorganism on a substrate under copolymer-accumulating conditions wherein i) said microorganism is an alcohol-utilising Alcaligenes eutrophus strain, that is capable of accumulating poly B hydroxybutyric acid; ii) said substrate comprises a source of assimilable carbon; iii) said substrate comprises a primary alcohol, other than methanol, having an odd number of carbon atoms; and iv) said copolymer-accumulating conditions comprise a period of cultivation under growth-limiting conditions such that said microorganism accumulates at least 10% by weight of copolymer.

2. A process according to claim 1 wherein said primary alcohol, other than methanol, having an odd number of carbon atoms is propan-1-ol.

3. A process according to either claim 1 or claim 2 wherein that carbon present in said primary alcohol, other than methanol, having an odd number of carbon atoms is at least 10% by weight of the total amount of carbon present in said substrate.

4. A process according to claim 3 wherein that carbon present in said primary alcohol, other than methanol, having an odd number of carbon atoms, is at least 25% by weight of the total amount of carbon present in said substrate.

5. A process according to any one of claims 1 to 4 wherein said microorganism is Alcaligenes eutrophus CBS

388.76 or Alcaligenes eutrophus NCIB 12080 6. A process according to any one of claims 1 to 5, which comprises in a first stage culturing the alcohol-utilising Alcaligenes eutrophus strain on an assimilable carbon source in an aqueous medium comprising sufficient of an assimilable nitrogen source to support a concentration of at least 14 14 gl-1 of non-copolymcr cell material and in a subsequent second stage containina culturing under conditions of nitrogen starvation. o-s e:0r&ee~ e \eSNe. 7. Alcaligenes eutrophus NCIB 12080 or an alcohol-utilising mutant thereof. 8. A process for preparing Alcaligenes eutrophus NCIB 12080 or an alcohol-utilising mutant thereof which comprises cultivating the strain Alcaligenes eutrophus NCIB 11599 initially under oxygen limitation conditions, and subsequently under carbon limitation conditions on a substrate comprising glucose, wherein during cultivation under carbon limitation conditions a progressively increasing proportion of ethanol is added to said substrate until such time as the substrate consists of ethanol. 9. A pure culture of Alcaligenes eutrophus NCIB 120801or an alcohol-utilising mutant thereof in the presence of a primary alcohol, other than methanol, having an odd number S of carbon atoms. A process according to claim 1 substantially as hereinbefore described with reference to any one of the examples. DATED: 10 October 1989 ‘a .PHILLIPS ORMONDE AND FITZPATRIC’ N Attorneys for: t IMPERIAL CHEMICAL INDUSTRIES PLC MC T t MJP i 1

AU57825/86A
1985-05-28
1986-05-22
Poly beta-hydroxybutyric acid/poly beta-hydroxyvaleric acid copolymer production

Ceased

AU601681B2
(en)

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GB8513310D0
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1985-05-28
1985-05-28
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1985-05-28

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1990-09-20

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Poly beta-hydroxybutyric acid/poly beta-hydroxyvaleric acid copolymer production

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Cited By (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU637657B2
(en)

1989-12-08
1993-06-03
Metabolix, Inc.
Co-polymer production

Families Citing this family (17)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

EP0288908B1
(en)

1987-04-28
1992-10-21
Mitsubishi Gas Chemical Company, Inc.
Process for production of a random copolymer comprising d-(-)-3-hydroxybutyrate units and d-(-)-3-hydroxyvalerate

US5245023A
(en)

1987-06-29
1993-09-14
Massachusetts Institute Of Technology
Method for producing novel polyester biopolymers

US4876331A
(en)

1987-08-18
1989-10-24
Mitsubishi Kasei Corporation
Copolyester and process for producing the same

ATE129524T1
(en)

1989-05-02
1995-11-15
Zeneca Ltd

PRODUCTION OF COPOLYMERS.

US5264546A
(en)

1989-05-02
1993-11-23
Imperial Chemical Industries Plc
Copolymer production

US5371002A
(en)

1989-06-07
1994-12-06
James Madison University
Method of production of poly-beta-hydroxyalkanoate copolymers

WO1991013207A1
(en)

1990-02-21
1991-09-05
Pulp And Paper Research Institute Of Canada
POLY-β-HYDROXYALKANOATES FOR USE IN FIBRE CONSTRUCTS AND FILMS

CA2076038C
(en)

1990-02-21
2001-03-27
Robert Henry Marchessault
Poly.beta.hydroxyalkanoates for use in fibre constructs and films

GB9011777D0
(en)

1990-05-25
1990-07-18
Ici Plc
Hv/hb copolymer production

EP0475785A3
(en)

1990-09-14
1993-04-14
Mitsubishi Gas Chemical Company, Inc.
Process for preparation of copolymer

AT395319B
(en)

1990-10-05
1992-11-25
Danubia Petrochem Polymere

METHOD FOR OBTAINING A POLYHYDROXYALKANOATE FROM THE CELL MATERIAL OF A MICROORGANISM AND POLYHYDROXYALKANOATE FLAKES

US5569595A
(en)

1991-09-27
1996-10-29
Center For Innovative Technology
Production of poly-β-hydroxybutyrate in prokaryotic host cells

DE4433134A1
(en)

1994-09-16
1996-03-21
Buck Chem Tech Werke

Process for the preparation of polyhydroxy fatty acids and recombinant bacterial strains for carrying out the process

NL1011431C2
(en)

1999-03-03
2000-09-05
Univ Delft Tech

Process for producing polyhydroxyalkanoate.

TW200420726A
(en)

2002-10-10
2004-10-16
Kaneka Corp
Process for producing copolyester

EP2284261B1
(en)

2008-04-23
2017-03-29
Toyota Jidosha Kabushiki Kaisha
Method for production of polyester copolymer using genetically modified microorganism

JP5738594B2
(en)

2008-10-27
2015-06-24
トヨタ自動車株式会社

Method for producing polylactic acid using recombinant microorganisms

Citations (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU5560780A
(en)

1979-02-21
1980-08-28

Monsanto Company

Production of polyhydroxybutyric acid from methylbacterium organopnilum

Family Cites Families (4)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU560653B2
(en)

1981-07-07
1987-04-16
Monsanto Company
3-hydroxybutyrate polymers

GB8301344D0
(en)

1983-01-18
1983-02-16
Ici Plc
Poly(beta-hydroxybutyric acid)

GB8311677D0
(en)

1983-04-28
1983-06-02
Ici Plc
Extraction process

DE3343551A1
(en)

1983-12-01
1985-06-13
Lentia GmbH Chem. u. pharm. Erzeugnisse – Industriebedarf, 8000 München

METHOD FOR THE BIOTECHNOLOGICAL PRODUCTION OF POLY-D (-) – 3-HYDROXYBUTTERIC ACID

1985

1985-05-28
GB
GB858513310A
patent/GB8513310D0/en
active
Pending

1986

1986-05-09
DE
DE8686303558T
patent/DE3682328D1/en
not_active
Expired – Fee Related

1986-05-09
EP
EP86303558A
patent/EP0204442B1/en
not_active
Expired – Lifetime

1986-05-09
AT
AT86303558T
patent/ATE69267T1/en
not_active
IP Right Cessation

1986-05-12
GB
GB868611523A
patent/GB8611523D0/en
active
Pending

1986-05-16
ZA
ZA863661A
patent/ZA863661B/en
unknown

1986-05-19
IN
IN445/DEL/86A
patent/IN167933B/en
unknown

1986-05-22
NZ
NZ216268A
patent/NZ216268A/en
unknown

1986-05-22
AU
AU57825/86A
patent/AU601681B2/en
not_active
Ceased

1986-05-23
CA
CA000509813A
patent/CA1313635C/en
not_active
Expired – Fee Related

1986-05-27
BR
BR8602397A
patent/BR8602397A/en
not_active
Application Discontinuation

1986-05-28
JP
JP61123214A
patent/JPH0779705B2/en
not_active
Expired – Lifetime

Patent Citations (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU5560780A
(en)

1979-02-21
1980-08-28
Monsanto Company
Production of polyhydroxybutyric acid from methylbacterium organopnilum

Cited By (1)

* Cited by examiner, † Cited by third party

Publication number
Priority date
Publication date
Assignee
Title

AU637657B2
(en)

1989-12-08
1993-06-03
Metabolix, Inc.
Co-polymer production

Also Published As

Publication number
Publication date

JPS61293385A
(en)

1986-12-24

NZ216268A
(en)

1989-04-26

ATE69267T1
(en)

1991-11-15

CA1313635C
(en)

1993-02-16

ZA863661B
(en)

1987-02-25

AU5782586A
(en)

1986-12-04

BR8602397A
(en)

1987-01-21

EP0204442A3
(en)

1987-10-07

GB8611523D0
(en)

1986-06-18

GB8513310D0
(en)

1985-07-03

EP0204442A2
(en)

1986-12-10

IN167933B
(en)

1991-01-12

JPH0779705B2
(en)

1995-08-30

EP0204442B1
(en)

1991-11-06

DE3682328D1
(en)

1991-12-12

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