Process for producing C9, C11 and C13 alkanols and microorganism capable of same

Abstract: Described is a microbiological method for producing C 9 , C 11 and C 13 alkanols defined according to the structures: wherein R 1 is methyl or n-propyl using ketones defined according to the generic structure: as a substrate and using the novel microorganism: Pseudomonas cepacia ATCC 55792 or mutants thereof. Also described is the novel mixture of alcohols of this invention defined according to the structures: wherein R 1 is methyl or n-propyl and flavor and fragrance uses thereof.

Description: The present invention concerns biologically pure cultures of the microorganism: Pseudomonas cepacia ATCC 55792 capable of producing in high yields with high conversions at least one mixture of alkanols containing the compounds defined according to the generic structures: (the mixture having an optical rotation of between about +0.2 and about +0.9° due to the presence of optical isomers defined according to the structure: with the major proportion of the composition being those compounds defined according to the structure: and with compounds defined according to the structure: being optical isomers having optical rotations of between about +3 and about +4° under aerobic conditions and in an aqueous medium containing at least one ketone defined according to the generic structure: wherein R 1 is methyl or n-propyl. In carrying out the reaction using Pseudomonas cepacia ATCC 55792 (or a mutant thereof), the following reaction takes place: more specifically, shown thusly: By way of example, our invention contemplates processes defined by the following reactions: (1) using Pseudomonas cepacia ATCC 55792 (or a mutant thereof): and and (2) purification reactions for purification of the resulting products: and In view of the impurities contained in the resulting crude reaction products: (wherein the structure: represents a mixture and in the fixture one of the dashed lines represents a carbon carbon double bond and the other of the dashed lines represents a carbon carbon single bond). The structures shown thusly herein: and are for the "dextrorotatory(+)" optical isomers of the compounds having the structures: and The form in which the microorganism is used is not critical. It can be used as the culture (suspension), i.e., including the cells and the corresponding nutrient solution, or in the form of cells suspended in a buffer solution. The cells, or an enzyme extract thereof, may be immobilized on a suitable solid support, which may then be used to effect transformations. The suspended culture mixture is prepared by inoculation of a suitable aqueous nutrient medium with the microorganism (or a mutant thereof). A suitable nutrient medium is one which contains nitrogen sources, inorganic salts, growth factors, the desired substrate(s) and, optionally, other carbon sources. Some carbon sources suitable for use in the inventive process include, for example, glucose, galactose, L-sorbose, maltose, sucrose, cellobiose, trehalose, L-arabinose, L-rhamnose, ethanol, glycerol, L-erythrithol, D-mannitol, lactose, melibiose, raffinose, melezitose, starch, D-xylose, D-sorbitol, a-methyl-D-glucoside, lactic acid, citric acid and succinic acid. Suitable nitrogen sources include, for example, nitrogen-containing organic substances such as peptone, meat extract, yeast extract, corn steep liquor, casein, urea, amino acids, or nitrogen-containing inorganic compounds such as nitrates, nitrites and inorganic ammonium salts. Suitable inorganic salts include, for example, phosphates of magnesium, potassium, calcium or sodium. The above-mentioned culture medium nutrients may be supplemented with, for example, one or more vitamins of the B group and/or one or more trace minerals such as Fe, Mo, Cu, Mn and B, as desired. The vitamins of trace minerals are not necessary when a small amount of yeast extract is added to the medium. Addition of an antibiotic, such as chloroamphenicol or chlorotetracycline, may be desirable when bacterial contamination is a problem. The cultivation of the microorganism may be carried out as a stationary culture or as a submersed (e.g., shaking culture, fermentation culture) under aerobic conditions. One may suitably work in the pH range of from between 2.5 and about 9.0 and preferably in the range of between about 3.0 and about 7.5 and most preferably between about 3.0 and about 6.5. The pH may be regulated by the addition of inorganic or organic acids such as hydrochloric acid, acetic acid and oxalic acid, or by the addition of bases such as sodium hydroxide and ammonium hydroxide, or by the addition of a buffer such as a phosphate or a phthalate. The incubation temperature should suitably be maintained between about 12°C and about 33°C, with a range between about 15°C and about 30°C being more preferred, and a range between about 18°C and about 28°C being most preferred. The process according to this invention may be conveniently carried out by adding one or a mixture of the ketones having the structure: to the nutrient medium at the onset of cultivation as the sole carbon source. Alternatively, the substrate may be added in combination with another carbon source, such as dextrose, either during cultivation or when the carbon source is depleted. The only restriction on the concentration of substrate in the culture medium is that of being able to effectively aerate the culture. However, the substrate concentration is preferably in the range of between about 0.1 g/L and about 100 g/L, more preferably in the range of between about 0.5 g/L and about 50 g/L, and most preferably in the range of between about 2.5 g/L and about 30 g/L. The transformation can be suitably carried out under any of the above-mentioned conditions. The total transformation time (after initial cultivation period) may vary depending on the composition of the nutrient medium and the substrate concentration. In general, shaking flask cultures require from between about 12 hours and about 264 hours. However, when a fementor is used, the cultivation time may be reduced to about 48 hours or less. Additional conditions of the transformation as shown by the reaction: are: (a) a temperature in the range of from about 20°C up to about 45°C, preferably from about 25°C up to about 40°C, and most preferably from about 25°C up to 30°C at a pressure of from about zero psig (atmospheric) up to about 15 psig; (b) a pH range of from about 5.0 up to about 8.5, preferably from about 6.0 up to about 8.0, and most preferably from about 6.5 up to about 7.5; and (c) an aeration range of from about 0.1 up to about 1.5 v/v/m of air at 1 atmosphere pressure (liter per liter per minute). The transformation may be carried out using the cells of the microorganism isolated from the culture solution, with an enzyme extract isolated from the cells in a manner well known to the art. In this case, the transformation can be conveniently carried out in a variety of aqueous nutrient mediums including, for example, in a buffer solution, in a physiological salt solution, in a fresh nutrient solution or in water. The isolated cells or enzyme extract may be immobilized on a solid support and the desired transformation effected. Also, transformation of the substrate may be effected by mutants of this organism. Such mutants can be readily obtained by methods well known in the art, for example, by exposing the cells to UV or X-rays, or known mutagenic substances such as, for example, acridine orange, and are readily obtained as will be seen from Example I-M, infra The substrate can be added to the medium as a powder, or a slurry in an emulsifier such as TWEEN® 80 (polyoxyethylenesorbitan monostearate), or as a solution in an emulsifier, or as a solution in a hydrophilic solvent such as acetone, methanol, ethanol, ethylene glycol, propylene glycol or dioxan. A surface-active agent or a dispersion agent can also be added to an aqueous suspension of the substrate, or the substrate can be emulsified using ultrasound. Conventional antifoam agents, such as silicone oils (e.g., UCON®), polyalkyleneglycol derivatives, maize oil or soya oil, can be used to control foaming. The transformation of the substrate can be monitored using standard analytical techniques such as GLC, TLC, HPLC, IR and NMR. If a rapid disappearance of the substrate is observed, more substrate can then be added in order to maximize the transformation capacity of the microorganism. The process is generally terminated when most of the substrate has disappeared from the culture medium. The compounds having the structures: may be recovered from the aqueous nutrient medium as set forth in the Examples, infra, and as set forth below. Isolation and purification of the compounds defined according to the structures: from the fermentation broths may be achieved by initially using conventional techniques including filtration or centrifugation, solvent extraction, distillation, crystallization and the like, and then carrying out a further purification (as exemplified in Example XVIII, infra) using, for example, the reactions: and The mixture of compounds as defined according to the structures: may be used for their organoleptic (flavor or fragrance) properties "as is" or they may be further distilled. The microorganism employed in this invention was isolated form a soil sample obtained from central New Jersey, the United States of America. The strain has been deposited with the American Type Culture Collection with the accession number as follows: Pseudomonas cepacia ATCC 55792 (initially submitted to the American Type Culture Collection as IFF-8296C). This isolate is a member of the Pseudomonas RNA Group II. The principal feature shared by the species in this group is nutritional versatility in the type and number of organic compounds utilized as sole sources of carbon and energy, which include carbohydrates, mono- and dicarboxylic acids, mono- and polyalcohols, aromatic compounds, amino acids and amines. The most outstanding property of RNA Group II is the fact that, with the exception of Pseudomonas pickettii , the species included are animal or plant pathogens [ Bergey's Manual of Systematic Bacteriology, Volume 1, N.R. Krieg (ed.), Williams & Wilkins, 1984.] Growth occurs in mineral base medium containing ammonium ions as sole source of nitrogen and glucose as sole source of carbon and energy. A few strains fail to produce indophenol oxidase, and others produce a slow and very weak indolphenol oxidase reaction. The majority of the strains are not susceptible to antibiotics of the polymyxin class. Pseudomonas cepacia was first described as a phytopathogen that causes sour skin, an onion bulb rot. It has wide geographic distribution and has been isolated from raw and pasteurized milk; hard lens and soft lens wetting and saline solutions; nasal sprays; rotting tree trunk; forest soil, muck soil; soil enrichments; and natural river and tap waters. Pseudomonas cepacia has also been isolated from a variety of clinical materials. It is an opportunistic pathogen, and most infections are of nosocomial origin. Pseudomonas cepacia demonstrates a multiple antibiotic resistance pattern, especially to the aminoglycosides usually active against Pseudomonas aeruginosa. Pseudomonas cepacia produce pathological changes in animals similar to those produced by Pseudomonas pseudomallei [G.L. Gilardi, 1985. Pseudomonas, pages 361-362. In E.H. Lennette, A. Balows, W.J. Hausler, Jr., and H.J. Shadomy (ed.), Manual of Clinical Microbiology, 4th edition, American Society for Microbiology, Washington, D.C.]. Strain exhibits the minimal characters for the identification of Pseudomonas cepacia strains (see Table I). Strain is identified as Pseudomonas cepacia . Morphology: This strain is a gram-negative; short rod. Cells occur singly and in pairs. It is motile by means of a tuft of polar flagella [lophotrichous, that is, three or more flagella]. In nitrogen deficient medium, cells accumulate poly-β-hydroxybutyrate as a carbon reserve material; this is a typical feature of Pseudomonas cepacia. Colonies showed the following characteristics in nutrient medium (ATCC medium #3): Circular, entire margin smooth, glistening; convex elevation and butyrous in consistency. Strain did not have any pigmentation. R.Y. Stanier, N.J. Palleroni and M. Doudoroff in their study of 19 strains of Pseudomonas cepacia found 2 strains which were completely non-pigmented [R.Y. Stanier, N.J. Palleroni and M. Doudoroff, 1966. "The Aerobic Pseudomonads: A Taxonomic Study," J. Gen. Microbiol., 43:247-253]. Many strains of clinical origin are non-pigmented [G.L. Gilardi, 1985. Pseudomonas, page 361. In E.H. Lennette, A. Balows, W.J. Hausler, Jr. and H.J. Shadomy (ed.), Manual of Clinical Microbiology, 4th edition, American Society for Microbiology, Washington, D.C.]. Pigmentation is not correlated with any other phenotypic characters studied and, therefore, seem to be devoid of taxonomic significance. Biochemical and Physiological Properties: IFF-8296C is oxidase and catalase positive. Gelatin and starch are not hydrolyzed. Caesin is hydrolyzed and gave a positive lecithinase (egg yolk) reaction. Strain grows on MacConkey agar, but not on 0.05% centrimide agar. Denitrification is negative; nitrate is reduced to nitrite. Growth occurs at 42°C, 37°C, 30°C, 26°C, but not at 4°C. Metabolism is by respiration (aerobic). Strain is lipolytic [TWEEN® 80 hydrolysis]. Strain is lysine decarboxylase positive. Acid is produced from all Hugh and Leifson's O-F Medium, except in L-rhamnose, adonitol, inulin and salicin which were alkaline. N.J. Palleroni and B. Holmes in their studies of Pseudomonas cepacia found that some strains hydrolyze gelatin and some give a positive lecithinase reaction [N.J. Palleroni and B. Holmes, October 1981. Pseudomonas cepacia Sp. nov., nom. rev., International Journal of Systematic Bacteriology, 31:479-481]. Palleroni, et al tested 19 strains and found that 16 strains hydrolyzed gelatin, and one gave a negative egg yolk reaction [R.Y. Stanier, N.J. Palleroni and M. Doudoroff, 1966. The Aerobic Pseudomonads: A Taxonomic Study, J. Gen. Microbiol., 43:247-253] (see Table II). Nutritional Properties: No organic growth factors are required. Nutritionally, IFF-8296C is very versatile. Most of the organic compounds can be used as sole carbon and energy sources for growth. These compounds include a large variety of carbohydrates, mono- and dicarboxylic acids, mono- and polyalcohols, aromatic compounds, amino acids an amines. Lactose, maltose, L-rhamnose, adonitol, erythritol, geraniol, acetamide, testosterone, citraconate, L-(+)-tartrate, glycine, DL-norleucine, M-hydroxybenzoate, D-tryptophan, butylamine, mesaconate and methanol were not utilized by IFF-8296C for growth. Palleroni, et al in their studies of 19 strains of Pseudomonas cepacia found 5 strains which lacked a series of nutritional characters otherwise practically constant for the group. One strain in their studies appeared to be the most defective in the whole collection: it was unable to grow in practical, universal substrates used by the group [R.Y. Stanier, N.J. Palleroni and M. Doudoroff, 1966. "The Aerobic Pseudomonads: A Taxonomic Study," J. Gen. Microbiol., 43:247-253] (see Table II). Antibiotic Susceptibilities: The antibiotic susceptibilities of IFF-8296C as determined by standardized, single-disk diffusion tests was determined using 28 different antibiotics. IFF-8296C was resistant to 15 antibiotics tested, susceptible to 10 antibiotics and intermediate to 3 antibiotics. Antibiotic susceptibilities of Pseudomonas cepacia is from the studies of H.A. Sinsabaugh and G.W. Howard, Jr. [Henry A. Sinsabaugh and G.W. Howard, Jr., International Journal of Systematic Bacteriology, April 1975, pages 187-201]. Fifteen (15) strains of Pseudomonas cepacia were tested for antibiotic susceptibility (see Table III). MINIMAL CHARACTERS FOR IDENTIFICATION OF PSEUDOMONAD CEPACIA STRAINS Characters Sign ± % Positive IFF-8296C Polar tuft of 3 or more flagella per pole + 99 + Motility + 99 + O-F glucose medium, open, acid + 100 + O-F lactose medium, acid + 98 + O-F maltose medium, acid + 97 + O-F mannitol medium, acid + 100 + Nitrate to gas - 0 - L-lysine decarboxylase + 90 + L-arginine dihydrolase - 0 - *G.L. Gilardi, 1985, Pseudomonas, page 361. In E.H. Lennette, A. Balows, W.J. Hausler, Jr. and H.J. Shadomy (editor), Manual of clinical Microbiology, 4th edition, American Society for Microbiology, Washington, D.C. GENERAL CHARACTERISTICS OF PSEUDOMONAS CEPACIA Characteristics P. cepacia Type Strain IFF-8296C Numer of flagella >1 >1 >1 Organic growth factor requirement - - - Oxidase reaction + + + Poly-β-hydroxybutyrate accumulation + + + Gelatin hydrolysis d + - Starch hydrolysis - - - Lecithinase (egg yolk) d + + Lipase (TWEEN® 80 hydrolysis) + + + Denitrification - - - Reduction of nitrate to nitrite + - + Lysine decarboxylase + + + Growth at 4°C - - - Growth at 42°C + + + Carbon Sources Used for Growth: D-xylose d + + D-ribose + + + L-rhamnose d - - Mesaconate - - - Erythritol - - - Malonate + + + Adipate + + + Benzoate + + + D-alanine + + + L-valine v + + ANTIBIOTIC SUSCEPTIBILITIES OF IFF-8296C Antibiotic Potency P . cepacia IFF-8296C R S I R S I Amikacin 30 - - - S Ampicillin 10 93% 7% 0% R Carbenicillin 100 73% 27% 0% S Cefamandole 30 - - - R Cefotaxime 30 - - - S Cefoxitin 30 - - - R Cephalothin 30 100% 0% 0% R Chloramphenicol 30 7% 73% 20% S Clindamycin 2 - - - R Colistin 10 93% 7% 0% R Erythromycin 15 100% 0% 0% R Furadantin 100 - - - R Gentamycin 10 - - - I Kanamycin 30 - - - S Methicillin 5 100% 0% 0% R Nafcillin 1 - - - R Nalidixic acid 30 27% 60% 13% I Neomycin 30 60% 13% 27% S Novobiocin 30 - - - S Oxicillin 1 - - - R Penicillin 10 units 100% 0% 0% R Polymixin B 300 - - - R Streptomycin 10 - - - R Tetracycline 30 93% 0% 7% I Trimethoprim/ Sulfamethoxazole 1.25/23.75 - - - S Tobramycin 10 - - - S Sulfisoxazole .25 - - - S Vancomycin 30 - - - R PHYSIOLOGY AND BIOCHEMISTRY: Gram positive - TWEEN® 80 hydrolysis + Gram negative + Indole - Gram variable - Simmons citrate growth + Motile + Urease + Flagella peritrichous - Nitrate to nitrite + Flagella lophotrichous + Nitrite reduction - Flagella monotrichous - Nitrite to nitrogen gas - Flagella lateral - Hydrogen sulfide (TSI) - 4 C growth - Lysine decarboxylase + 26 C growth + Arginine (Mollers) - 30 C growth + Ornithine decarboxylase - 37 C growth + Phenylalanine deamination - 42 C growth + Lecithinase + Fluorescein produced - Phosphatase + Pyocyanine produced - Catalase + Diffusible orange - Oxidase + Diffusible yellow - Gluconate oxidation - Diffusible purple - Growth on malonate as SCS + Non-diffusible green - Tyrosine degradation + Other non-diffusible pigments - dl-hydroxybutyrate growth + Melanin pigment produced - PHB accumulation + pH 6.0 growth + Growth on 0.05% cetrimide - 3% NaCl growth + Growth on acetate as SCS + 6.5% NaCl growth - Testosterone degradation - MacConkey agar growth + 1% NaCl growth + Skim milk agar growth + Mucoid growth on glucose agar - Aesculin hydrolysis - 0.1% TTC growth + Casein hydrolysis + 0.2% TTC growth + Starch hydrolysis - Litmus milk acid + Gelatinase - Litmus milk peptonized + TWEEN® 20 hydrolysis + REACTIONS IN HUGH & LEIFSON'S MEDIUM: Acid from: Acid from: L-arabinose + D-mannose + cellobiose + L-rhamnose K ethanol + D-ribose + D-fructose + sucrose + D-glucose AO 2 + trehalose + D-glucose AnO 2 - D-xylose + Alkaline pH in D-glucose - adonitol K Acid from: dulcitol + glycerol + D-galactose + i-inositol + inulin K lactose + salicin K maltose + D-sorbitol + D-mannitol + Control K K = alkaline SOLE CARBON SOURCE IN STANIER'S MINERAL BASE: L-arabinose as SCS + 2-ketogluconate as SCS + cellobiose as SCS + DL-lactate as SCS + D-fructose as SCS + L-malate as SCS + D-glucose as SCS + pelargonate as SCS + lactose as SCS - propionate as SCS + maltose as SCS - quinate as SCS + D-mannitol as SCS + succinate as SCS + L-rhamnose as SCS - L-+-tartrate as SCS - D-ribose as SCS + valerate as SCS + D-sorbitol as SCS + B-alanine as SCS + sucrose as SCS + D-A-alanine as SCS + trehalose as SCS + betaine as SCS + D-xylose as SCS + glycine as SCS - adonitol as SCS - L-histidine as SCS + erythritol as SCS - DL-norleucine as SCS - glycerol as SCS + L-proline as SCS + ethanol as SCS + D-tryptophan as SCS - geraniol as SCS - L-valine as SCS + i-inositol as SCS + DL-arginine as SCS + sebacic acid as SCS + benzylamine as SCS + acetamide as SCS - butylamine as SCS - adipate as SCS + putrescine as SCS + benzoate as SCS + mesaconate as SCS - butyrate as SCS + DL-glycerate as SCS + citraconate as SCS - L-tryptophan as SCS + D-gluconate as SCS + Methanol as SCS - M-hydroxybenzoate as SCS - SCS = Sole Carbon Source REFERENCES: 1. Bergey's Manual of Systematic Bacteriology, Vol. 1, N.R. Krieg (ed.), Williams & Wilkins, 1984. 2. Gilardi, G.L., 1985, Pseudomonas, pages 361-362, In E.H. Lennette, A. Balows, W.J. Hausler, Jr., and H.J. Shadomy (ed.), Manual of Clinical Microbiology, 4th Edition, American Society for Microbiology, Washington, D.C.. 3. Palleroni, N.J., B. Holmes, October 1981, Pseudomonas cepacia, sp. nov., nom. rev. International Journal of Systematic Bacteriology, 31, pages 479-481. 4. Sinsabaugh, H.A. and G.W. Howard, Jr., April 1975, "Emendation of the Description of Pseudomonas cepacia Buckholder" (synonyms: Pseudomonas multivorans Stanier, et al, Pseudomonas kingae Jonsson; EO-I Group), International Journal of Systematic Bacteriology, pages 187-201. 5. Stanier, R.Y., N.J. Palleroni and M. Doudoroff, 1966, "The Aerobic Pseudomonads : A Taxonomic Study," J. Gen. Microbiol., 43, pages 247-253. 6. F.W. FORNEY ET AL.: 'Bacterial oxidation of 2-Tridecanone to 1-Undecanol' J. BACTERIOL., Vol. 93, no.2, February 1967 (1967-02), pages 649-655, XP000892165 AM. SOC. MICROBIOL., BALTIMORE, US; 7. F.W. FORNEY AND A.J. MARKOVETZ: 'A enzyme system for aliphatic methyl ketone oxidation' BIOCHEM. AND BIOPHYS. RES. COMMUNICATIONS, vol. 37, no. 1, 1969, pages 31-38, XP000892171 ACADEMIC PRESS, NEW YORK, US 8. US-A-4 588 584 (LUMSDEN ROBERT D ET AL) 13 May 1986 (1986-05-13) 9. US-A-4 975 277 (JANISIEWICZ WOJCIECH J ET AL) 4 December 1990 (1990-12-04) 10. A. BOSETTI ET AL.: 'Production of primary aliphatic alcohols with a recombinant alkane hydroxylase enzyme system' ENZYMES AND MICROBIAL TECHNOLOGY, vol. 14, September 1992 (1992-09), pages 702-708, XP000892168 BUTTERWORTH-HEINEMANN, MA, US The mixture of alcohols of this invention defined according to the structures: wherein R 1 is methyl or n-propyl can be added to flavor and/or perfume compositions in a pure form, or they can be added to mixtures of materials in flavor and/or fragrance imparting compositions to provide a desired organoleptic or fragrance character to the finished flavor or perfume material (as the case may be). The flavor, perfume and fragrance compositions obtained according to this invention are suitable in a wide variety of foodstuffs and perfumed articles and can also be used to improve, enhance, modify, alter or reinforce natural flavor and fragrance materials. It will thus be appreciated that the mixture of alcohols of this invention are useful as olfactory agents and fragrances or organoleptic agents and flavors. According to the present invention, there is provided a biologically pure culture of the microorganism, Pseudomonas cepacia ATCC 55792. The present invention also provides a biologically pure culture containing the microorganism, Pseudomonas cepacia ATCC 55792, being capable of producing a mixture of compounds defined according to the generic structures: with a major proportion of the composition being those compounds defined according to the structure: with the compound defined according to the structure: being optical isomers having an optical rotation of between about +3 and about +4° in a recoverable quantity upon the transformation of a compound defined according to the structure: wherein R 1 is, in the alternative, methyl or n-propyl. The invention also provides a process for producing a mixture of alkanols defined according to the structures: containing at least 65 mole percent of the alkanol defined according to the structure: comprising the step of admixing at least one alkanone defined according to the structure: with the organism: Pseudomonas cepacia ATCC 55792 or a mutant thereof wherein R 1 is, in the alternative, n-propyl or methyl. The present invention additionally provides a mixture of compounds having the structures: wherein R1 is, in the alternative, methyl or n-propyl; and wherein the mixture has an optical rotation of between about +0.2 and about +0.9°. The following Examples I-XVIII serve to illustrate embodiments of the invention for production and purification of the mixture of alcohols and alcohols per se of our invention as it is now preferred to practice it. Examples XIX, XX and XXI indicate uses of the mixture of alcohols of our invention for their organoleptic properties. It will be understood that these examples are illustrative and the invention is to be considered restricted thereto only as indicated in the appended claims. EXAMPLE I NATURAL NONYL ALCOHOL PRODUCTION USING PSEUDOMONAS CEPACIA ATCC 55792 INOCULUM PREPARATION: (i) Medium 0.1% NH 4 NO 3 ; 0.1% KH 2 PO 4 ; 0.05% MgSO 4 .7H 2 O; 0.2% TASTONE® 900 (yeast extract, Trademark of Red Star BioProduct Division of Universal Food Corporation of 433 East Michigan Street, Milwaukee, Wisconsin 53201); and 0.05% TWEEN® 80. The pH of the resulting mixture is adjusted to 6.5 prior to sterilization. After sterilization, add 1% hexadecane to the flask. (ii) Inoculum 2 Ml of medium is used to wash a slant of Pseudomonas cepacia ATCC 55792. Then the wash is used to inoculate 100 ml of media. (iii) Conditions Temperature: 28°C; Agitation: 150 RPM; and Incubation time: 24 hours. PRODUCTION: 10 Liters of the following medium was prepared in a 14 liter fermenter and sterilized at 121°C for 20 minutes: Production Medium Ingredient Grams per Liter NH 4 NO 3 1.0 KH 2 PO 4 1.0 MgSO 4 .7H 2 O 0.5 TASTONE® 900 2.0 TWEEN® 80 0.5 After sterilization, the fermenter was inoculated with 100 ml of 24 hour-grown inoculum produced, supra. 200 Grams of natural 2-undecanone was then added to the resulting mixture in the fermenter with stirring. PROCESS PERAMETERS: Temperature: 30°C; Aeration: 0.4 v/v/m; and Agitation: 800 RPM. The pH of the reaction mass is automatically controlled at 6.5 using 20% aqueous ammonia. After 6 days while maintaining the fermentation at 30°C and the pH at 6.5, 75 grams of 87% pure nonyl alcohol was recovered by steam distillation directly the fermenter. The remaining product is dextrorotatory 2-undecanol having the structure: The resulting product is fractionally distilled yielding the following fractions: Fraction Number Vapor Temperature (°C) Liquid Temperature (°C) Vacuum mm/Hg Pressure Reflux Ratio 1 20/23 23/110 200 100% 2 115 135 350 100% 3 128 138 400 9:1 4 128 138 400 9:1 5 130 135 400 9:1 6 131 135 400 9:1 7 131 138 400 9:1 8 132 138 400 9:1 9 132 138 400 9:1 10 132 138 400 9:1 11 132 139 400 9:1 12 132 138 400 9:1 13 132 138 400 9:1 14 132 138 400 9:1 15 132 138 400 9:1 16 132 138 400 9:1 17 133 138 400 9:1 18 132 138 400 9:1 19 132 138 400 9:1 20 132 138 400 9:1 21 132 138 400 9:1 22 132 138 400 9:1 23 132 138 400 9:1 24 133 140 400 9:1 25 133 140 400 9:1 26 133 142 400 9:1 27 133 145 400 9:1 28 133 145 400 9:1 29 133 145 400 9:1 30 132 145 400 9:1 31 132 148 400 9:1 32 132 150 400 9:1 33 132 152 400 9:1 34 148 155 400 9:1 35 148 155 400 9:1 36 150 158 400 9:1 37 148 158 400 9:1 38 146 166 400 9:1 39 145 165 400 9:1 40 133 220 400 9:1 Fractions 9-33 are bulked. Bulked distillation fractions 9-33 contain the compound having the structure: and the compound having the structure: as confirmed by NMR, IR and mass spectral analyses. The resulting product is used for its organoleptic utilities as set forth in Examples XIX, et seq., infra. EXAMPLE I-M FORMATION OF MUTANTS OF PSEUDOMONAS CEPACIA ATCC 55792 (1) Medium 0.2% TASTONE® 900; 0.1% NH 4 NO 3 ; 0.1% KH 2 PO 4 ; 0.05% MgSO 4 .7H 2 O; and 0.05% TWEEN® 80. The pH of the resulting medium is adjusted to 6.5 prior to sterilization using sodium hydroxide. After sterilization, 1% sterile CERELOSE® 2001 is added to the mixture. (2) A 500 ml flask containing 100 ml of the above medium (produced according to step 1) was inoculated with 2 ml of a frozen culture of Pseudomonas cepacia ATCC 55792. This flask is then incubated at 28°C with shaking at 150 RPM for 18-24 hours. (3) A 500 ml flask containing 100 ml of the above medium (produced according to step (1)) was inoculated with 10 ml of the culture produced according to step (2) above and incubated for 4 hours. (4) 2 ml of the 4-hour culture produced according to step (3) were centrifuged and the resulting cell pellet was washed twice with 2 ml of sterile 0.1 M sodium phosphate buffer (pH = 7.0). (5) The resulting pellet produced according to step (4) was suspended in 1 ml of buffer and 50 µl ethyl methanesulfonate (EMS produced by Eastman Kodak Corporation of Rochester, New York) was added. The suspension was then placed on a rotating platform and incubated for 1 hour at 28°C. (6) Mutagenesis was terminated by the addition of 8 ml of 5% sodium thiosulfate to 0.2 ml of the EMS-treated cells. Serial dilutions of this culture were plated on the following two media and incubated at 28°C for 48 hours: (a) the medium of step (1) with 2% agar added; and (b) the medium of step (1) with 2% agar added, except that the dextrose is replaced with 95% foodgrade ethanol. (7) Colonies which grew on the sugar-containing medium, but did not grow on the ethanol-containing medium (ethanol negative) were isolated for reaction. Three different isolates thus produced were used in Examples IV, VI and IX, infra, respectively. EXAMPLE II The above reaction is carried out in the same manner as in Example I, except that the dextrose was replaced with 1% undecanone in the inoculum flask. After 6 days, 67.2 grams of 82.6% of pure nonyl alcohol was recovered through steam distillation with the remainder being the optical isomer having the structure: EXAMPLE III The foregoing reaction was carried out in the same manner as in Example II, except that, initially, the pH was maintained at 7.5 and the aeration rate was 0.1 v/v/m. After 88 hours, the pH was lowered to 6.5 and the aeration rate was increased 0.4 v/v/m. After 10 days, 66 grams of 87% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the optical isomer having the structure: EXAMPLE IV The foregoing reaction was carried out in the same manner as in Example I, except that a mutant of Pseudomonas cepacia ATCC 55792 produced according to Example I-M was used. After 10 days, 83 grams of 91.9% pure nonyl alcohol was recovered through steam distillation with the remainder being the optical isomer having the structure: EXAMPLE V The foregoing reaction was carried out in the same manner as in Example I, except that 0.25% sterile glucose solution was added to the fermenter at the time of inoculation. The undecanone was then added 18 hours later. After 7 days, 100 grams of 85.5% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the optical isomer having the structure: EXAMPLE VI The foregoing reaction was carried out in the same manner as in Example V, except that the mutant produced according to Example I-M, supra, was used. After 13 days, 96.5 grams of 85.0% pure nonyl alcohol was recovered through steam distillation with the remainder being the stereo isomer having the structure: EXAMPLE VII The foregoing reaction was carried out in the same manner as in Example V, except that 0.5% sterile glucose solution was used. After 5 days, 80.0 grams of 89.7% pure nonyl alcohol was recovered through steam distillation with the remainder being the stereo isomer having the structure: EXAMPLE VIII The foregoing reaction was carried out in the same manner as in Example V, except that 0.375% sterile glucose solution was used and the inoculum was grown on 1% sugar. After 6 days, 93.8 grams of 92.9% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the stereo isomer having the structure: EXAMPLE IX The foregoing reaction was carried out in the same manner as in Example VIII, except that a mutant prepared according Example I-M was used. After 7 days, 87.8 grams of 77.3% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the stereo isomer having the structure: A distillation cut containing 72% 1-nonanol and 18% 2-undecanol has an optical rotation of +0.73°. EXAMPLE X The foregoing reaction was carried out in the same manner as in Example VIII, except that when the undecanone was added to the fermenter, the aeration rate was reduced to 0.1 v/v/m and back pressure was set at 10 psig. After 9 days, 97.4 grams of 46.9% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the stereo isomer having the structure: A distillation cut containing 50% 1-nonanol and 37% 2-undecanol had an optical rotation of +0.24°. A distillation cut containing 96% 2-undecanol and 3.6% 2-undecanone had an optical rotation of +3.44°. EXAMPLE XI The foregoing reaction was carried out in the same manner as in Example VIII, except that when the undecanone was added to the fermenter, the aeration rate was reduced to 0.1 v/v/m and the temperature was lowered to 25°C. After 7 days, 84.5 grams of 87.8% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the stereo isomer having the structure: EXAMPLE XII The foregoing reaction was carried out in the same manner as in Example XI, except that instead of adding all of the 2-undecanone at once, it was slowly pumped into the fermenter over a 24-hour period. After 7 days, 43.9 grams of 77.1% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the stereo isomer having the structure: EXAMPLE XIII The foregoing reaction was carried out in the same manner as in Example VIII, except that after 24 hours, the cooling water to the condenser was turned off and a charcoal trap was connected to the fermenter exhaust line. After 5 days, 92.8 grams of 90% pure nonyl alcohol was recovered from the fermenter during steam distillation with the remainder of the product being the stereo isomer-having the structure: Nothing was recovered from the charcoal trap. EXAMPLE XIV The foregoing reaction was carried out in the same manner as in Example XIII, except that 20% aqueous sodium hydroxide was used for maintaining the pH throughout the fermentation. After 6 days, 100.5 grams of 88.3% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the stereo isomer having the structure: EXAMPLE XV The foregoing reaction was carried out in the same manner as in Example XIV, except that 5 grams per liter of TASTONE® 900 was used in the fermenter. After 5 days, 23.6 grams of 72.4% pure nonyl alcohol was recovered through steam distillation with the remainder of the product being the stereo isomer having the structure: EXAMPLE XVI An 800 liter batch was carried out in the same manner as in Example V, except that 50% aqueous sodium hydroxide was used for maintaining the pH throughout the fermentation. After 8 days, a total of 6.95 kg of crude nonyl alcohol with a purity of 94.4% was recovered by steam distillation. The nonyl alcohol was further purified by fractional distillation as set forth in Example I yielding fractions boiling at a vapor temperature of 132-133°C and a liquid temperature of 138-150°C at a pressure of 400 mm/Hg. The remainder of the product is the optical isomer having the structure: EXAMPLE XVII 100 ml of inoculum medium is placed in a 500 ml flask. The inoculum medium is sterilized in the flask at 121°C for a 20-minute period. After sterilization, 1% tridecanone having the structure: and 1% of 24 hour-sugar-grown inoculum were added to the reaction mass. The resulting culture is placed in an incubator-shaker operated at 150 RPM at 28°C for a period of 72 hours. The contents of the flask were then extracted with ethyl acetate and the solvent was then removed under vacuum. A total of 0.42 grams of crude extract containing 85.4% undecanol having the structure: and 10.5% tridecanone having the structure: was obtained. The remainder of the mixture is the stereo isomer having the structure: (as confirmed by NMR, IR and mass spectral analyses). A distillation cut containing 99% 2-undecanol at an optical rotation of +3.44°. EXAMPLE XVIII PURIFICATION OF NATURAL NONYL ALCOHOL The crude, extracted, natural nonyl alcohol of Example XVI contained as the major impurity 2-undecanol having the structure: These two materials readily separate by distillation. However, the product also contained a small amount of unsaturated C-9 amine having the structure: which is a mixture of compounds wherein in the mixture one of the dashed lines is a carbon carbon double bond and the other of the dashed lines is a carbon carbon single bond. This unsaturated C-9 amine boils very closely to the main component. It can degrade flavor quality if not removed. In addition, the presence of small amounts of residual methly nonyl ketone having the structure: as well as related ketones can cause a problem during the purification. Even though these ketones are higher boiling than nonyl alcohol, they co-distill. Accordingly, using the reactions: and these impurities can be removed. Thus, the amine impurity in the crude is easily removed by extraction with dilute acid such as hydrochloric acid. Other acids such as citric acid and acetic acid can also be used. The methyl nonyl ketone and isomers thereof, if over 1% in the crude (compared to the nonyl alcohol), must be chemically converted to the corresponding cyclic ketal via reaction with 1,2-propylene glycol as set forth in the above reaction. The corresponding dioxylane derivative is higher boiling than the 2-undecyl alcohol and can be readily separated by distillation. To accomplish this, the crude reaction mixture is reacted with 1,2-propylene glycol in the presence of paratoluene sulfonic acid in boiling cyclohexane. The ketal (dioxolane) made from ethylene glycol is not high boiling enough. While these ingredients are not "flavor natural" per se, they do not react in any way with nonyl alcohol. They react solely with with the ketonic side products. PROCEDURE Materials: Crude nonyl alcohol produced according to Example XVI, quantity ... 1,740 grams; Cyclohexane ... 1,500 grams; Paratoluene sulfonic acid ... 5 grams; 1,2-Propylene glycol ... 50 grams; 5% aqueous hydrochloric acid ... 500 ml; and 5% aqueous sodium hydroxide solution ... 1,000 ml. Equipment: 5 Liter flask is equipped with an overhead stirrer, Bidwell trap, condenser, heating mantle, thermometer, sepatory funnel and 18" x 1.5" Goodloe packed column. Action: (1) The crude-washed nonyl alcohol is extracted once with 500 ml of 5% aqueous hydrochloric acid to remove acid notes. The acid wash should precede the ketal formation step. Dilute acid can partially hydrolyze the ketal-releasing free methyl nonyl ketone; (2) The organic layer is charged to the flask along with the cyclohexane, the propylene glycol and the paratoluene sulfonic acid. The solution is heated at reflux for 2 hours, separating out any water formed; (3) The organic layer is cooled and washed with 5% aqueous sodium hydroxide. The resulting product has a GC-capillary survey as set forth in Figures 4A and 4B; and (4) The crude product, weighing 2,896 grams and having a total ion chromatogram as set forth in Figure 3, is charged to the still. The solvent is removed at atmospheric pressure to a pot temperature of 120°C. The pressure is slowly reduced to 400 mm/Hg. The resulting product is distilled off at a reflux ratio of 9:1, boiling at 132°C to a final pot temperature of 160°C. 35 Fractions were collected. Fractions 9-33 were bulked and flavor approved. EXAMPLE XIX The following composition is prepared: The addition of the mixture of compounds having the structures: prepared according to Example I improve the overall citrus/floral quality of the instant formulation, lending a more neroli oil-like and coriander-like effect thereto. Thus, the fragrance can be described as: "a citrus and floral aroma having neroli oil-like and coriander topnotes". EXAMPLE XX COSMETIC POWDER PREPARATION A cosmetic powder is prepared by mixing in a ball mill 100 grams of talcum powder with 0.25 grams of one of the substances set forth in Table IV below containing the mixture of compounds having the structures: Each of the cosmetic powders has an excellent aroma as described in Table IV below. EXAMPLE XXI Three meatloaf-type products are prepared according to the following formulation: Ingredients Amounts TVP® minced 1 cup Ground beef 1 cup Water 1 cup Beef suet 1/2 cup Bread crumbs, dry and unflavored 1 cup Whole milk 1 cup Egg albumen 3 tablespoons Salt 1.25 tablespoons Black pepper 0.25 tablespoons Catsup 0.25 tablespoons Water 32 ml Three separate portions prepared according to the foregoing formulation are made into three meatloaves. Loaf A contains no additional additive. Loaf B contains 32 ml of fresh pressed onion juice to replace the 32 ml of water. Loaf C contains 0.6 ppm of the mixture of the compound having the structure: prepared according to Example II and, in addition, 32 ml of fresh pressed onion juice to replace the 32 ml of water. The three loaves are baked at 350°F for 1 hour and evaluated for flavor by a panel of twelve judges. The consensus of the judges is that Loaf C is superior to Loaves A and B. The onion/baked goods character of Loaf C enhances the overall taste and covers the dry, cardboard-like cereal character of Loaf A. It is accordingly apparent that the product of this invention is a valuable ingredient for a wide variety of flavors and types of foodstuffs. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1A is the GC-capillary survey for the reaction product of Example I containing the compounds having the structures: (conditions: 50 meter x 0.32 mm x 0.5 micrometer methyl silicon (OV-1) column programmed from 75-225°C at 2°C per minute). Figure 1B is a GC-capillary survey for the reaction product of Example I containing the compounds having the structures: (conditions: 50 meter x 0.32 mm x 0.3 mm CARBOWAX® 20M column programmed from 75-225°C at 2°C per minute). Figure 1C is the total ion chromatogram for the reaction product of Example I containing the compounds having the structures: and (conditions: methyl silicon (OV-1) column programmed from 75-225°C at 2°C per minute). Figure 2A is a GC-capillary survey for the reaction product of Example XVII containing the compounds having the structures: (conditions: 50 meter x 0.32 mm x 0.5 micrometers methyl silicon (OV-1) column programmed from 75-225°C at 2°C per minute). Figure 2B is a GC-capillary survey for the reaction product of Example XVII containing the compounds having the structures: (conditions: 50 meter x 0.32 mm x 0.3 micrometers CARBOWAX® 20M column programmed from 75-225°C at 2°C per minute). Figure 2C is a total ion chromatogram for the reaction product of Example XVII containing the compounds having the structures: (conditions: OV-1 (methyl silicon) column programmed from 75-225°C at 2°C per minute). Figure 3 is a total ion chromatogram for the crude product of Example XVIII containing the compounds having the structures: (representing a mixture of compounds wherein in the mixture, one of the dashed lines represents a carbon carbon single bond and the other of the dashed lines represents represents a carbon carbon double bond); Figure 4A is a GC-capillary survey for the purified product of Example XVIII containing the compounds having the structures: (conditions: 50 meter x 0.32 mm x 0.5 micrometers methyl silicon (OV-1) column programmed from 75-225°C at 2°C per minute). Figure 4B is a GC-capillary survey for the purified product of Example XVIII containing the compounds having the structures: (conditions: 50 meter x 0.32 mm x 0.5 micrometers CARBOWAX® 20M column programmed from 75-225°C at 2°C per minute). DETAILED DESCRIPTION OF THE DRAWINGS Referring to Figure 1A, the GC-capillary survey for the product of Example I, the peak indicated by reference numeral 10 is for the compound having the structure: Referring to Figure 1B, the GC-capillary survey for the product of Example I, the peak indicated by reference numeral 11 is for the compound having the structure: Referring to Figure 1C, the total ion chromatogram for the reaction product of Example I, the peak indicated by reference numeral 12 is for the compound having the structure: The peak indicated by reference numeral 13 is for the compound having the structure: The peak indicated by reference numeral 14 is for the compound having the structure: The peak indicated by reference numeral 15 is for the compound having the structure: The peak indicated by reference numeral 16 is for the compound having the structure: Referring to Figure 2A, the GC-capillary survey for the reaction product of Example XVII, the peak indicated by reference numeral 20 is for the compound having the structure: Referring to Figure 2B, the GC-capillary survey for the reaction product of Example XVII, the peak indicated by reference numeral 21 is for the compound having the structure: Referring to Figure 2C, the total ion chromatogram for the reaction product of Example XVII, the peak indicated by reference numeral 22 is for the compound having the structure: The peak indicated by reference numeral 23 is for the compound having the structure: The peak indicated by reference numeral 24 is for the compound having the structure: The peak indicated by reference numeral 25 is for the compound having the structure: The peak indicated by reference numeral 26 is for the compound having the structure: The peak indicated by reference numeral 27 is for the compound having the structure: Referring to Figure 3, the total ion chromatogram for the crude product of Example XVIII, the peak indicated by reference numeral 30 is for the compound having the structure: The peak indicated by reference numeral 31 is for the compound having the structure: The peak indicated by reference numeral 32 is for the mixture of compounds defined according to the structure: wherein in the mixture in one of the compounds, one of the dashed lines is a carbon carbon double bond and the other of the dashed lines is a carbon carbon single bond. The peak indicated by reference numeral 33 is for the compound having the structure: The peak indicated by reference numeral 34 is for the compound having the structure: The peak indicated by reference numeral 35 is for the compound having the structure: The peak indicated by reference numeral 36 is for the compound having the structure: Referring to Figure 4A, the GC-capillary survey for the purified product of Example XVIII, the peak indicated by reference numeral 41A is for the compound having the struture: The peak indicated by reference numeral 42A is for the compound having the structure: Referring to Figure 4B, the GC-capillary survey for the purified product of Example XVIII, the peak indicated by reference numeral 41B is for the compound having the structure: The peak indicated by reference numeral 42B is for the compound having the structure: The features disclosed in the foregoing description, in the following claims and/or in the accompanying drawings may both separately and in any combination thereof, be material for realising the invention in diverse forms thereof.

Claims: A biologically pure culture of the microorganism, Pseudomonas cepacia ATCC 55792. A biologically pure culture containing the microorganism, Pseudomonas cepacia ATCC 55792, being capable of producing a mixture of compounds defined according to the generic structures: with a major proportion of the composition being those compounds defined according to the structure: with the compound defined according to the structure: being optical isomers having an optical rotation of between about +3 and about +4° in a recoverable quantity upon the transformation of a compound defined according to the structure: wherein R 1 is, in the alternative, methyl or n-propyl. A process for producing a mixture of alkanols defined according to the structures: containing at least 65 mole percent of the alkanol defined according to the structure: comprising the step of admixing at least one alkanone defined according to the structure: with the organism: Pseudomonas cepacia ATCC 55792 or a mutant thereof wherein R 1 is, in the alternative, n-propyl or methyl. The process according to Claim 3 comprising the additional step of intimately admixing with a consumable material an aroma or taste augmenting, enhancing or imparting quantity of the resulting product, in order to augment or enhance the aroma or taste of the consumable material. The process of Claim 3 comprising the additionalsteps of purifying the resulting product by admixing therewith first an acid to cause the reaction: to proceed and then with propylene glycol to cause the reaction: to proceed whereby in the compound having the structure: one of the dashed lines is a carbon carbon double bond and the other of the dashed lines is a carbon carbon single bond. A mixture of compounds having the structures: wherein R 1 is, in the alternative, methyl or n-propyl; and wherein the mixture has an optical rotation of between about +0.2 and about +0.9°. The mixture of Claim 6 wherein the compound having the structure: has an optical rotation of between about +3 and about +4°. A process for augmenting, enhancing or imparting an aroma or taste in or to a consumable material which is, in the alternative, a perfume composition, a perfumed article or a foodstuff, comprising the step of intimately admixing with said consumable material an aroma augmenting, enhancing or imparting quantity and concentration of the mixture of Claim 6.

Inventors: FARBOOD MOHAMAD I, KIZER LAURA E, MCLEAN LYNDA B, SPRECKER MARK A, FARBOOD, MOHAMAD I., KIZER, LAURA E., MCLEAN, LYNDA B., SPRECKER, MARK A.
Applicants: INT FLAVORS & FRAGRANCES INC, INTERNATIONAL FLAVORS & FRAGRANCES INC.
Application year: 1998
Main classification: C12N1
IPC codes: A23L1, C12P7, C11D3, A61K8, A61Q13, C12N1