Biochemical Society Transactions 690 21. Cliffe, A. J. & Law, B. A. (1990) Food Chem. 36, 73-80 22. Neviani, E., Boquien, C. Y., Monnet, V., Phan Thanh, L. & Gripon, J.-C. (1989) Appl. Environ. Microbiol. 55,2308-23 14 23. Desmazeaud, M. J. & Zevaco, C. (1979) Milchwissenschaft 34,606-6 10 24. Tan, P. S. T. & Konings, W. N. (1990) Appl. Environ. Microbiol. 56,526-532 25. Exterkate, F. A. & de Veer, G. J. C. M. (1987) Appl. Environ. Microbiol. 53, 577-583 26. Niven, G. W. (1991) J. Gen. Microbiol. 137, 1207-12 12 27. Law, B. A. (1979)J. Appl. Bacteriol. 46, 455-463 (1981) Agric. Biol. Chem. 45, 159-165 29. van Boven, A,, Tan, P. S. T. & Konings. W. N. (1988) Appl. Environ. Microbiol. 54, 43-49 30. Bosman. B. W., Tan, P. S. T. & Konings, W. N. (1990) Appl. Environ. Microbiol. 56, 1839- 1843 31. Booth, M., Fhaolain, I. N.. Jennings, P. V. & O’Cuinn, G. (1990)J. Dairy Kes. 5 7 , 8 9 4 9 32. Zevaco, C., Monnet, V. & Gripon, J.-C. (1990)J. Appl. Bacteriol. 68. 357-366 33. Kiefer-Partsch, B., Bockelmann, W., Geis, A. & Teuber, M. (1989) Appl. Microbiol. Biotechnol. 31, 75-78 34. Booth, M., Jennings, P. V., Fhaolain, I. N. & O’Cuinn, G., (1990)J. Llairy Res. 57,245-254 35. Yan, T. K., Azuma, N., Kaminogawa, S. & Yamauchi. K. (1987) Appl. Environ. Microbiol. 53,2296-2302 36. Yan, T. K., Azuma, N., Kaminogawa, S. & Yamauchi, K. (1987) Eur. J. Biochem. 163,259-265 37. Kaminogawa, S., Ninomiya, T. & Yamauchi. K. (1984)J. Dairy Sci. 67,2483-2492 38. Exterkate, F. A. (1985)J. Dairy Sci. 68, 562-571 Received 12 April 1991 Micro-organisms as a novel source of flavour compounds Mohamad 1. Farbood International Flavours & Fragrances, Union Beach, N] 07735, U.S.A. Consumer demand for natural flavour ingredients for foods and beverages has resulted in substantial research in production of these ingredients via processes which are considered to be natural. A number of research papers and patents describing these approaches have been published [ 1-31. In this paper, the use of micro-organisms for commercial production of natural flavour compounds is discussed. Appropriate micro-organisms may be obtained from the many culture collections based on information available in the literature or can be isolated from nature using selective screening techniques. A survey of disclosed commercial processes reveals that in most cases a natural precursor was used which is closely related structurally to the product. De nouo biosynthesis from substrates such as carbohydrates, acetate, etc., in most cases has not resulted in viable commercial processes. In other words, it seems that controlled catabolic transformation of a precursor is preferred over de nouo biosynthetic pathways for production of natural flavour compounds. The historical development of industrial biotechnology may be divided into four eras [4]:(1) production of foods, such as wine, beer, vinegar, cheese, yogurt, bread, etc.; (2) large-scale production of specific materials under non-sterile conditions (e.g., organic acids, solvents, biomass, etc.), by relatively simple technology; (3) production under Volume 19 sterile conditions, of relatively expensive secondary metabolites by more complex processes (e.g., penicillin); and (4) application of modern scientific developments in biotechnology, e.g., enzyme research, gene technology, molecular biology and process engineering. Enzyme research has led to processes involving immobilized enzymes and whole cells. Application of developments in the field of molecular biology and gene technology have led to processes using micro-organisms with specifically altered gene structure. Process engineering has led to the development of new reactors, optimization of processes, and better measurement and control of process parameters. In the near future bioengineering advances may lead to computer control of entire production processes from inoculation to product recovery. There are several requisites for industrial micro-organisms [ 51: purity, genetic stability, amenability to change by mutagenic agents, facile formation of reproductive units, acceptable growth rate, and relatively short process time for product accumulation. In addition, if possible, the strain should protect itself against contamination, be capable of long-term culture maintenance, and ideally, minimize or eliminate production of all toxic substances. Such micro-organisms may either be obtained from a culture collection or isolated from natural sources by screening programmes. Screening may Food Biotechnology be defined as the application of highly selective procedures to detect and isolate, from a large population, only those micro-organisms capable of producing the desired metabolite. The greatest challenges are to establish a suitable assay system and to determine the criteria for selection and isolation. Available information can be used as a guide, but the selection, isolation, and improvement of cultures still rest mainly on empirical experience. Identification of isolated micro-organisms allows a comparison with those already described in the literature. Such properties as production of desirable fermentation products, pathogenicity for plants, animals, or humans, and special precautions for handling such organisms must be considered. Identification allows one, to a certain extent, to predict growth characteristics and other requirements which need to be considered in the study of the isolated micro-organism. These approaches to commercially successful microbiological processes can be illustrated with a few examples taken from the patent literature and some of our own work. The information available in published research can lead to development of a commercial process in a relatively short period of time. Production of methyl anthranilate is a good example. Transformation of 4-(methylamino)benzaldehyde to 4-aminobenzaldehyde using Polyp o r n versicolor (Fig. l), had been described previously [6]. From this work it was evident that Polyporus species and related micro-organisms were capable of N-demethylation reactions. This property was used to advantage in the Ndemethylation of methyl N-methylanthranilate [7]. However, commercially acceptable yields could only be achieved by optimization of growth conditions and substrate levels, and choice of appropriate emulsifiers. Two disadvantages to this process are the lengthy incubation time and the limited availability of methyl N-methylanthranilate. In another approach to this compound via a bacterial process, anthranilic acid is produced in high yield using I.tryptophan as the substrate [#]. The acid is subsequently esterified with methanol in a second process. Disadvantages to this approach are the availability of natural methanol and the need for the additional esterification step. Another example of the use of published information to develop a commercial process for flavour compounds in the production of esters by Geotrichum fragrans [9]. This organism, originally identified as Oospora suaveolans, was reported to produce small amounts of ‘fruity’ esters [lo]. An extensive strain development programme resulted in substantial improvement in yield of esters. Selection of the appropriate amino acid precursor, deduced from analysis of the esters produced and knowledge of amino acid degradation pathways, directed ester production to the most desirable compounds. Ultimately, commercially feasible yields of esters were achieved by continuously sweeping volatile products from the fermentation in the air stream and trapping them on activated carbon. Obviously, this necessitated development of an effective process for recovery of the product from the carbon. Thus, one can see that in this case commercial success resulted from a combination of several factors most of which could not be foreseen at the inception of the project. The possible formation of these esters from isoleucine was postulated (Fig. 2). In some cases, a soil screening programme and published information may be combined to Fig. 2 Postulated mechanism for formation of ethyl esters via isoleucine degradation pathway Fig. I CH&H,$MX(NH&CKlH CH, N-demethylation activity of Polyporus versicolor NH-CH, Q- CH3CHzOH versicolor CHO CHO 4-(methylamino)benzaldehyde 4-aminobenzaldehyde COOCH, NH-CH, 0 H&H,G-OCH&H, I 0 Polyporus P 0 CH,CH=C-C-S-CoA I CH,CH&SCoA Polyporus versicolor Methyl N-methylanthranilate CH,-CCH-C-SCoA Methylanthranilate 1991 69 I Biochemical Society Transactions 692 develop a viable process [ 111. Numerous recently published research and issued patents describe the production of y-decalactone, an important component of many fruit flavours. In essence, most of these processes are similar to that described in US. Patent 4,560,656 [ 113. Obviously these patents differ by employing different micro-organisms. Although the first organism was isolated through soil screening using castor oil or ricinoleic acid as the sole carbon source, the underlying scientific principle of this process was published in 1963 describing the metabolism of ricinoleic acid by members of the Cundzifu genus [ 121. In this paper, appearance and disappearance of 4-hydroxydecanoic acid during catabolism of ricinoleic acid by Cundzifu guilliermondi was reported. The patented process is very straightforward, using a member of the Cundzifu genus and castor oil as substrate. However, the thought processes that went into this work demonstrate the underlying complexity. An organism was needed with lipase activity, and one that preferably could tolerate high levels of free fatty acid. A medium (‘chemical environment’) was needed that allowed the growth of the micro-organism, but kept most of the released fatty acids, including the product acid, in ionic form to perhaps minimize their toxicity. Finally, using the concept of co-oxidation, a small quantity of decanoic acid added at the right time further increased the accumulation of y-hydroxydecanoic acid. A similar approach using Cundia petrophilum was devised to produce a mixture of saturated and unsaturated y-decalactones at a very high yield [ 131. In a recent patent application [ 141 a process is disclosed for production of 6- and y-octalactone. Members of the Mucor genus were employed and octanoic acid or its esters was used as substrate. Interestingly enough, these organisms differ from Cundzifu species in their fatty acid metabolism. Mucor species, besides possessing the normal poxidation pathway, hydroxylate the acid at the yposition. It seems in both cases that the bulkiness of the hydroxyl group at the y-position slows down the degradation of this acid resulting in its accumulation. In the development of micro-organisms for production of natural flavour compounds one may use selective soil screening to isolate a parent strain and then, via a combination of mutagenesis and screening techniques, isolate a strain capable of accumulating the desired product. A published process for the production of acetophenone is a good example of this approach [15]. A parent strain was Volume 19 isolated from soil by selective enrichment using cinnamic acid as the primary carbon source in a liquid minimal medium. Purified isolates were screened simultaneously for adaptation to benzoic acid, assuming that benzoic acid would be an intermediate in cinnamic acid degradation. Isolates were mutated with N-methyl-N-nitro-N-nitrosoguanidine and mutants which grew well on benzoic acid and poorly on cinnamic acid were selected and purified. The mutant which accumulated the highest levels of acetophenone was characterized by the American Type Culture Collection as an unclassified Pseudomonus sp. (ATCC 53716). The parent strain differs from the mutant in the distribution of 3-0x0-phenylpropionic acid between the two alternative branches namely formation of acetophenone and degradation via benzaldehyde. Transformation of sclareol (Z-ethenyldecahydro-2- hydroxy - 2 a , 5,5,8a-pentamethyl- 1-naphthalenepropanol) to related ambergris-like compounds has been of interest for a long time. The target compound is Ambrox (dodecahydro3a,6,6,9a-tetramethyI-naphtho[2,1-b]furan), the most important odour component of ambergris. In a chemical process chromium or manganese oxidation is used to convert sclareol into sclareolide (decahydro- 3a,6,6,9a-tetramethyl-naphtho [2,l- b] furan-2( lH)-one). The resulting sclareolide is reduced to a diol (decahydro-2-hy droxy-2a,5,s,8atetramethyl-naphthalene-ethanol), and finally the diol is cyclized to Ambrox using a reagent such as p-toluene-sulphonyl chloride. The disadvantages of the first step of this process are low yield (40-SO%), disposal of spent heavy metals, and, above all, a limited supply of starting material. Using selective soil screening on a minimal medium and sclareol as the sole source of carbon, two isolates were obtained [ 161. Both isolates were classified by Centralbureau voor Schimmel Cultures and designated to be Hyphozymu roseoniger, a new species. The morphological characteristics of this microorganism are very unique; in liquid medium, growing on dextrose only a yeast-like form is present during the first few days of growth. With sucrose as the carbon source, a completely filamentous form appears; the two forms are completely interchangeable by alternating between dextrose and sucrose. The metabolic activity of the yeast form is also slightly different from that of the filamentous form. Optimization of conditions, use of the proper emulsifier, and reducing the substrate particles to optimum size, resulted in conversion of sclareol at a 2% level to the diol with a yield of 81%. The main disadvantage of this process is its long fermentation Food Biotechnology period. Nonetheless, this process was the first breakthrough in sclareol biotransformation. According to disclosed information, apparently, the rate of degradation of epi-sclareol by H. roseoniger is slower than that of sclareol. Various compounds were synthesized and tested for possible conversion by H roseon*er [16]. It is now evident that all of these compounds were converted to the final product. Another patent describes a similar process [ 171. A large scale selective soil screening programme using a minimal medium and sclareol as sole carbon source resulted in four isolates, identified as Cryptococcus albidus (ATCC 20918 & 20921) (sclareolide producer), Cryptococcus luurentii (ATCC 20920) and Bensingtonia czlziztu (ATCC 209 19) (diol producer). Cryptococcus ulbidus converts, quantitatively, as much as 150 g/l of sclareol powder to sclareolide crystals. The product is recovered by simple filtration and purified by conventional crystallization procedures. Several intermediates in the transformation of sclareol by C albdus were isolated, purified, and identified to determine the likely pathway. Rased on our own research and published information [ 161, a pathway for the transformation of sclareol to sclareolide is proposed (Fig. 3). The steps in this transformation are: allylic rearrangement, oxidation of primary alcohol to corresponding acid, hydroxylation at B-position, two carbon cleavage, BaeyerVilliger oxidation, hydrolysis of ester, further oxidation of primary alcohol to carboxylic acid and cyclization in situ to form lactone. It should be Fig. 3 Proposed pathway for transformation of sclareol to sclareolide by Cryptococcus albidus emphasized that identification of intermediates and speculation on possible metabolic pathways are not only of scientific interest, but also can be extremely important for optimization of the process and biotransformation of related or unrelated molecules to strengthen the protection of a patent. The initial interest in sclareolide was for use as a starting material for the fragrance material, Ambrox. Later, is was discovered [ 181 that sclareolide imparts mouthfeel, increases the saltiness of sodium chloride, covers the bitterness of potassium chloride and adds richness and creaminess to low fat ice cream. Sclareolide has recently achieved GRAS status (i.e. generally recognized as safe) for flavour applications. The processes decribed above are all based upon the usage of wild-type organisms or ‘classical’ mutants thereof. It is likely that the introduction of genetic engineering techniques will have a major impact on this field. However, one must keep in mind that cost limitation is an important factor in the introduction of gene technology into this area. The acceptable costs of many flavour and fragrance compounds are, for the most part, far lower than those for pharmaceutical products. In conclusion, the specific examples presented here describe commercially viable processes. These approaches have been shown to be applicable to the production of highly-valued natural flavour ingredients. Furthermore, the final example demonstrates that fermentation processes can be developed as viable alternatives to classical organic synthesis for flavour, fragrance, and other fine chemicals. 1. Mironowicz, A. & Siewinski, A. (1906) Acta Biotechnol. 6, 141-146 2. Scharpf, L. G., Seitz, E. W., Morris, J. A. & Farbood, M. I. (1986) ACS Symp. Ser. 317,323-346 3. Gatfield, I. I,. (1988) Food Technol. 42, 110-169 4. Rehm, H. J. & Reed, G . (1981) in Biotechnology (Rehm, H. J. & Reed, G., eds.), vol. 1, pp. 2-3, Verlag Chemie, Weinheim, Deerfield Beach, Florida & Basel 5. Hesseltine, C. W. & Haynes, W. C. (1973) Prog. Ind. Microbiol. 12, 1-2 6. Schmidt, A. & May, R. (1965) Hoppe-Seyler’s Z . Physiol. Chem. 340,283-286 7. Gregory, P., Scire, B. & Farbood, M. 1. (1989) PCT Int. Appl. WO 89 00,203 8. Takasago Perfumery KK (1990) Japanese Pat. J02135-093-A 9. Farbood, M. I., Morris, J. A. & Seitz, E. W. (1987) U S . Pat. 4,686,307 10. Hatteri, S., Yamaguchi, T. & Kanisawa, T. (1974) Proc. Int. Congr. Food Sci. Technol. 4th 1, 143-151 11. Farbood, M. I. & Willis, B. J. (1985) US. Pat. 4,560,656 1991 693 Biochemical Society Transactions 694 12. Okui, S., Uchiyama, M., Mizugaki, M. & Sugawara, A. (1063) Hiochim. Hiophys. Acta 70, 348-35 1 13. Farbood. M. I., Morris, J. A., Sprecker, M. A,. Hienkowski, I,. J., Miller, K. l’.? Vock, M. 11. & Hagedorn, M. I,. ( 1 990) US. Pat. 4,960,597 14. Gregory, 1’. & Eilerman, K.G. (1989) PCT Int. Appl. WO 8912-134A 15. Hilton, M. D. & Cain, W. J. (1990) Appl. Environ. Microbiol. 56.623-627 16. Farbood, M. I., Willis, H. J. & Christenson, 1’. A. (1086) S. African ZA 8.5 04,306 17. Farbood. M. I., Morris, J. A. & Lhwney, A. 1. (1000) U S . Pat. 4,970,163 18. Huckholz, I,., Farbood, M. I., Kossiakoff, N. & Scharpf, I,. G. (1990) 1J.S.Pat. 4,000,603 Keceived 12 April 1091 Anti-microbial substances produced by food associated micro-organisms Hans Horn and Christina Msrtvedt MATFORSK, Norwegian Food Research Institute, Osloveien I , N- I430 As, Norway Introduction Fermentative breakdown of carbohydrates results in a range of small molecular mass organic molecules which exhibit anti-microbial action, including lactate, propionate, acetate and ethanol. Conditions favouring the growth of bacteria producing these metabolic end products were discovered and used thousands of years ago and are still exploited in the production of a variety of products. They are employed in different manners, either as food additives after production in industrial fermentors, or produced in situ during fermentation of meat, vegetables and milk. Today there is considerable renewed interest in the use of naturally produced anti-microbial substances for food preservation and protection owing to the low energy demand of the fermentation process and the discovery of an abundance of additional anti-microbial activities associated with the fermentative microbes. Recombinant DNA technology has made it possible to identify and clone genes encoding these anti-microbials and electrotransformation has enabled the transfer of the genes to other bacteria, thus opening the era of tailormade starter cultures. The present paper will survey the antimicrobials produced by food associated microorganisms with the main emphasis on the lactic acid bacteria and related organisms. Metabolic end products Present knowledge suggests that the commonest form of anti-microbial activity expressed in foods is that associated with lactic, acetic and propionic acids. Lactic acid results from the metabolism of many different types of bacteria, primarily LactoAbbreviation used: 3-HPA, 3-hydroxypropanal. Volume 19 bacillus, Lactococcus, Leuconostoc and Pediococcus. Lactic acid is produced from breakdown of hexoses via the Embden-Meyerhof-Parnas pathway. Ideally, in homofermentative breakdown one mole of hexose gives rise to two moles of lactic acid and two moles of ATP. The anti-microbial action of lactic acid is only moderate. The acid produced lowers the pH and the growth of most spoilage and pathogenic organisms is inhibited to some extent. Lactic acid causes the leakage of hydrogen ions across the cell membrane. This results in acidification of the cell interior and inhibition of nutrient transport. The energy-yielding metabolism is not influenced [ 11. Lactic acid is the primary acid produced during fermentation of sausage, sauerkraut, olives, yoghurt, etc. In heterofermentative breakdown of sugars, the dissimilation proceeds via the pentosephosphate shunt. One mole of hexose gives rise to one mole of lactic acid, ethanol, CO, and ATP, respectively. However, oxidation of NADH + H + using alternative hydrogen acceptors (see below) sometimes leads to the formation of acetic acid and ATP instead of ethanol. Acetic acid is one of the most used anti-microbials from micro-organisms. Industrially it is produced through aerobic oxidation of ethanol by members of the genus Acetobacter. Acetic acid is mainly used as a food additive, in the form of vinegar. It is added as a preservative substance and a flavouring agent to many different foods including mayonnaise, dressings, pickles and mustard. Acetic acid has a wide range of inhibitory activity, inhibiting yeasts and moulds as well as bacteria. Its action cannot be explained by pH reduction alone. The undissociated form penetrates the cell and hereby exerts its inhibitory action, which is consistent with its anti-microbial activity increasing with decreasing pH values.
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