EP0569569A1

EP0569569A1 - METHOD FOR OBTAINING POLY-$g(b)-HYDROXY-OCTANOIC ACID

Info

Publication number: EP0569569A1
Application number: EP92923487A
Authority: EP
Inventors: Eric Ohleyer
Original assignee: Firmenich SA
Current assignee: Firmenich SA
Priority date: 1991-11-29
Filing date: 1992-11-13
Publication date: 1993-11-18
Also published as: JPH06505403A; WO1993011656A1; US5422257A

Abstract

L'acide poly-beta-hydroxy-octanoïque, produit d'utilisation variée, a été préparé par un procédé de fermentation aérobique de bactéries capables d'accumuler ledit acide, procédé consistant à ajouter au milieu de culture la solution nutritive, dans laquelle l'un des agents est limitatif de croissance, de manière à maintenir un taux de dilution compris entre environ 0,050 et 0,100 h-1. La biomasse, une fois séparée du milieu de culture, est mise en suspension dans l'acétone ou l'isopropanol et la masse cellulaire, après séparation et séchage, a été dissoute dans un solvant organique inerte non chloré. L'acide désiré est obtenu par évaporation du filtrat clair recueilli après séparation de la masse solide sous forme d'un film polymérique stable.Poly-beta-hydroxy-octanoic acid, a product of varied use, was prepared by a process of aerobic fermentation of bacteria capable of accumulating said acid, process consisting in adding to the culture medium the nutrient solution, in which the one of the agents is growth limiting, so as to maintain a dilution rate of between about 0.050 and 0.100 h-1. The biomass, once separated from the culture medium, is suspended in acetone or isopropanol and the cell mass, after separation and drying, has been dissolved in an inert non-chlorinated organic solvent. The desired acid is obtained by evaporation of the clear filtrate collected after separation of the solid mass in the form of a stable polymeric film.

Description

Process for obtaining poly-β-hydroxy-octanoic acid

Technical area

The invention relates to the field of organic synthesis. In particular, it relates to a new process for obtaining poly-β-hydroxy-octanoic acid, a polymer constituted by repeating units of formula + CH (C ₅ H ₁₁ ) - CH ₂ - C (0) - 0 ^ _n

process which allows the preparation of this acid with good yields and without significant degradation of the polymer.

The method of the invention is based on a method of extracting poly-β-hydroxy-octanoic acid from a culture of bacteria containing it using an organic solvent.

Prior art

Poly-hydroxy-alkanoic acids are storage compounds found in certain families of bacteria. It is in the cytoplasmic solution that these acids are deposited in the form of an aggregate when the cells are cultivated in a medium rich in carbon and in which one of the nutritive agents is growth-limiting.

Several methods of extraction of these acids have been described in the literature. They are particularly intended for obtaining poly-β-hydroxy-butanoic acid or poly-β-hydroxy-octanoic acid for which extraction has been suggested using chlorinated solvents, for example chloroform or methylene chloride from cells obtained by cold drying, more precisely by lyophilization. Examples of such methods are described in Appl. About. Microbiol., 55 (1989), 1949; Appl.

About. Microbiol, 54 (1988), 1977 and Appl. About. Microbiol., 45 (1983), 71.

The use of chlorinated solvents on freeze-dried biomass comes up against two major drawbacks. On the one hand, such solvents are to be avoided, as far as possible, in large-scale industrial operations for obvious reasons of environmental protection and, on the other hand, the lyophilization process is particularly expensive. . Statement of the invention

The present invention provides a new solution to this problem.

In its general principle, the process of the invention consists in fact in cultivating appropriate bacteria in an adequate nutritive medium. The bacteria are then separated after fermentation by usual techniques, for example by centrifugation, and the wet biomass thus obtained is dispersed in acetone or isopropanol or other dehydrating solvent known in the prior art. Thus, after separation, the still wet biomass is stirred in the organic dispersion solvent chosen until a homogeneous suspension is obtained. The separation of the solid cell mass from the suspension is carried out according to the usual methods, for example by decantation, filtration or centrifugation. A simple filtration using a Buchner filter allows the separation of the cells from the bacteria in the form of a now dry powder. Further drying can optionally be carried out by direct exposure to air of the separated solid.

It should be noted that, although the poly-β-hydroxy-octanoic acid is completely soluble in anhydrous acetone, the presence of water, even in very small quantities, makes the polymer perfectly insoluble. The extraction of poly-β-hydroxy-octanoic acid takes place in non-chlorinated organic solvents defined by the following group: acetone, methyl isobutyl ketone, diisopropyl ketone, diethyl ketone, ethyl acetate, propyl acetate, butyl acetate, diethyl ether, diisopropyl ether and tetrahydrofuran. Preferably, acetone or tetrahydrofuran is used. In the absence of water, these. solvents make it possible to completely dissolve the polymer obtained by simple stirring at ordinary temperature. The relative proportion of the mass of the dried cells with respect to acetone or tetrahydrofuran is between approximately 7.5 and 15% (weight / volume). By filtration of the suspension obtained and evaporation of the separated clear solution, the desired product is finally obtained in the form of a translucent polymer film, essentially consisting of poly-β-hydroxy-octanoic acid.

As indicated above, the intracellular formation of poly-β-hydroxy-alkanoic acids has been observed in many families of bacteria. In particular, the fermentation of bacteria of the genus

Pseudomonas, in a nutritive medium in which one of the agents is growth-limiting, gives rise to the formation of poly-β-hydroxy-octanoic acid. Such bacteria cultures can be obtained from depositaries such as the ATCC (American Type Culture Collection, Rockville, Maryland, USA) or the DSM (Deutsche Sammlung von Mikroorganismen, Gôttingen, Germany). Specifically, in the process of the invention, bacteria of one of the following strains were used: Pseudomonas oleovorans ATCC 29347, Pseudomonas sp. DSM 1650, and Pseudomonas citronellonis DSM 50332.

We observed that when the fermentation was carried out according to a continuous culture method, for example chemostat, by adding the solution of the nutrient agent to the fermentation medium, the dilution rate exerts a determining influence on the yields of poly acid. - β-hydroxy-octanoic formed. Thus, at dilution rates of between about 0.050 and 0.100 h ^-1 , the acid in question was obtained in an amount of 14-21 parts by weight per 100 parts of dry cell mass. This yield decreases rapidly at higher dilution rates, an unexpected phenomenon for which we cannot offer a satisfactory explanation.

The invention therefore also relates to a process for obtaining poly-β-hydroxy-octanoic acid by aerobic fermentation of bacteria capable of accumulating said acid when cultivated in a nutrient solution rich in carbon and in which one nutritive agents is growth limiting, characterized in that the nutritive solution is added to the culture so as to maintain a dilution rate of between approximately 0.050 and 0.100 h ^-1 , which is then separated from the biomass of the culture medium, that the separated biomass is suspended in acetone or isopropanol or other known dehydrating solvent, that the suspension obtained is filtered and the dried solid biomass is brought into contact with an inert organic solvent chosen from the group that here: acetone, methyl isobutyl ketone, diisopropyl ketone, diethyl ketone, ethyl acetate, propyl acetate, butyl acetate, diethyl ether, diisopropyl ether and tetrahydrofura Finally, separate the solid mass from the suspension obtained and finally evaporate the resulting clear solution. The invention is illustrated in more detail by the following examples, in which the temperatures are indicated in degrees centigrade and the abbreviations have the usual meaning in the art. Example 1

The particular fermentation conditions applied in this example are similar to those described in the literature. However, as will be described later, the reaction is carried out under steady state conditions, therefore with a constant concentration of biomass.

Bacteria of the Pseudomonas sp. DSM 1650 under aerobic conditions by adjusting the pH to 7.0 and the temperature of 32 °. The fermentation was carried out in a chemostat of 21 in a nitrogen-containing nutrient medium limiting growth, the composition of which was as follows (proportions expressed relative to 1 l of distilled water).

* this solution had the following composition (proportions expressed relative to 11 of IN HCl):

Igl FeS0 ₄ .7H ₂ 0 2.78

MnCl ₂ .4H ₂ 0 1.98 CoS0 .7H ₂ 0 2.81

CaCl ₂ .2H ₂ 0 1.67

CuS0 ₄ .5H ₂ 0 0.14

ZnS0 ₄ .7H ₂ 0 0.29

This nutrient solution was added to the fermentation medium so as to maintain the dilution rate at a value of 0.085 h ^-1 .

After reaching a steady state, i.e. a constant concentration of biomass and a complete consumption of carbon and nitrogen, the cell mass is stored in a tank before centrifugation (30 min), washed with demineralized water and centrifuged again.

The wet mass (51.5 g) harvested from 21 of culture was suspended in 250 ml of isopropanol and stirred at room temperature until a homogeneous suspension is obtained, then it is filtered using a Bύchner type filter and 12.4 g of dry cell mass was obtained after air drying.

This dry mass was suspended in 155 ml of acetone and stirred for 1 h at room temperature, then it was filtered.

The clear filtrate was finally evaporated in air to provide 2.43 g of a translucent polymer film. The polymer content of the cell mass was determined by gas chromatography of the methyl ester of β-hydroxy-octanoic acid obtained by methanolysis of the polymer [see for example Appl. About. Microbiol. 54 (1988), 1977]. The proportion of polymer was 20% by weight.

Example 2

A dried biomass was obtained according to the method described in the previous example.

12.6 g of this mass were suspended in 126 ml of acetone and stirred for 3 h at room temperature, then the suspension was filtered. The clear filtrate was evaporated under reduced pressure at a temperature not exceeding 40 ° and 2.63 g of polymer were thus collected. The molecular weight of the polymer was calculated by the following formula:

MW = 2.11. 10 ² . [η] W * according to Makromolekulare Chemie 176 (1975), 2655, in which MW represents the molecular weight and [η] defines the intrinsic viscosity as measured at 30 ° by a digital Brookfiêld viscometer. The polymer was solubilized at different concentrations in cyclohexanone. Other tests have been carried out by suspending the dried biomass in solvents other than acetone, for example methyl isobutyl ketone, diisopropyl ketone, diethyl ketone, ethyl acetate, propyl acetate, acetate butyl, diethyl ether or even diisopropyl ether.

Similar results have also been obtained by fermentation of strains other than Pseudomonas sp. DSM 1650. This is how Pseudomonas oleovorans ATCC 29347 and Pseudomonas citronellonis DSM 50332 were used. Example 3

A dried biomass was obtained according to the method described in Example 1. The nutrient solution had the following composition (proportions expressed relative to 1 l of distilled water). octanoic acid 15.12 g

NH ₄ C1 1.92 g

K ₂ HP0 ₄ 4.40 g

KH ₂ P0 ₄ 3.40 g MgS0 ₄ .7H ₂ 0 1.50 g

Na ₂ S0 ₄ 2.00 g solution of trace elements in HCl * 5.0 ml

Igl FeS0 ₄ .7H ₂ 0 2.78

MnCl ₂ .4H ₂ 0 1.98

CoS0 ₄ .7H ₂ 0 2.81 CaCl ₂ .2H ₂ 0 1.67

CuS0 .5H ₂ 0 0.14

ZnS0 ₄ .7H ₂ 0 0.29

The operation was carried out as indicated in Example 1, adding the nutritive solution to the fermentation medium so as to maintain the dilution rate at the value indicated in the following table. Poly-β-hydroxy-octanoic acid was thus obtained in the indicated proportions expressed as the content of the polymer in the cell mass.

(1) dilution rate

(2) poly-β-hydroxy-octanoic acid [parts by weight]

Claims

1. Method for obtaining poly-β-hydroxy-octanoic acid by extraction using an organic solvent from a biomass containing said acid and obtained by bacterial fermentation under aerobic conditions in a medium rich in carbon and in which one of the nutritive agents is growth limiting, characterized in that the biomass is brought into contact, in previously dried form, with an inert organic solvent chosen from the following group: acetone, methyl isobutyl ketone, diisopropyl ketone, diethyl ketone, acetate ethyl, propyl acetate, butyl acetate, diethyl ether, diisopropyl ether and tetrahydrofuran, the solid mass is separated from the suspension obtained and finally the resulting clear solution is evaporated.

2. Method according to claim 1 characterized in that the proportion of the dried biomass relative to acetone is between about 7.5 and 15% (weight / volume).

3. Method according to claim 1 characterized in that the proportion of the dried biomass relative to tetrahydrofuran is between about 7.5 and 15% (weight / volume).

4. Method according to claim 1 characterized in that the biomass is obtained by fermentation of bacteria of the genus Pseudomonas.

5. Method according to claim 4 characterized in that the biomass is obtained by fermentation of bacteria belonging to one of the following strains:

Pseudomonas oleovorans ATCC 29347, Pseudomonas sp. DSM 1650, and Pseudomonas citronellonis DSM 50332.

6. Method according to claim 1 characterized in that the biomass consists of a dried cell mass obtained by the addition of acetone or isopropanol to the wet cell mass followed by filtration and air drying of the solid mass separate.

7. Method for obtaining poly-β-hydroxy-octanoic acid by aerobic fermentation of bacteria capable of accumulating said acid when cultivated in a nutritive solution rich in carbon and in which one of the nutritive agents is growth limiting , characterized in that the nutrient solution is added to the culture so as to maintain a dilution rate of between approximately 0.050 and 0.100 h ^-1 , which is then separated from the biomass culture medium, which suspends the separated biomass in acetone or isopropanol, that the suspension obtained is filtered and the dried biomass is brought into contact with an inert organic solvent chosen from the group below: acetone, methyl isobutyl ketone, diisopropyl ketone, diethyl ketone, ethyl acetate, propyl acetate, butyl acetate, diethyl ether, diisopropyl ether and tetrahydrofuran, the solid mass is separated from the suspension obtained and finally the resulting clear solution is evaporated.