PROCESS FOR THE MICROBIOLOGICAL PRODUCTION OF OIL

Abstract: An improved process employing yeast for the production of oils is described. Yeast is cultivated in a medium containing a carbon nutrient source of one or more fatty acids having between 10 and 20 carbons. These fatty acids provide a means for improving the yield of synthesized oil and for controlling their glyceryl ester composition.

Description: PROCESS FOR THE MICROBIOLOGICAL PRODUCTION OF OIL The supply of naturall*-occurring glyceryl-ester oils (by which term it is meant also to include fats) is commonly subject to periods of scarcity which may elevate prices and/or disturb various segments of industry. In addition, the limited variety of such oils rcstricts their usefulness for many practices. It is therefore understandable that alternative supplies, sources and types of such oils have been investigated extensively. One of the more promising of these alternatives involves the cultivation of oil-synthesizing microorganisms. Many microorganisms -- including algae, bacteria, molds and yeasts -which can synthcsize oil in the ordinary course of cellular metabolism have been found. The basic process steps for this neans of producing oils are simple and uniform. All that is rcquired is that the microorganism be cultivated in a suitable culture medium to allow synthesis of the oil, then separated from the medium and treated for recovery of its intracellular content of oil. It is within the framework of these basic steps that most investigation has taken place. In particular, researchers have concentrated on secking to identify the combinations of specific microorganisms, media, and conditions which would permit economically practicable oil production. Despite extensive efforts, however, the most crucial deficiencies of microbiological oil production have remained. With few exceptions, microorganisms have produced dissappointing low yields of oil. Even the most successful microorganisms, for example, seldom reached oil contents of as much as 40% zy dry cell weight and the great majority had substantially lower yields. This fact, coupled with the difficulties of recovering the intracellularly stored oil, made the cost of this approach generally prohibitive. The drawbacks imposed by low yields, however, are further compounded by the inability to exert adequate control over the composition of the oil synthesized. If, for example, cercain of the known specialty oils or improved oils could be produced, the higher prices they could command might provide commercial justification for this approach. Thus far, however, no such general means of control has been discovered. In accordance with the present invention, it is possible Doth to improve the yield of oil synthesized by a microorganism and to exert substantial control over the chemical composition of that oil. By thus permitting high yields of preselected oils of particular importance, this invention renders the microbiological production of oils a commercial practicality. In its most general embodiment, this invention involves the discovery that the aerobic synthesis of oils by yeasts may be controlled by using certain fatty acids as the carbon nutrient source of their culture or fermentation media. These fatty acids, which have between 10 and 20 carbons, may act individually or collectively to increase oil yield and to cause synthesis of oil having a particular, preselected composition. In additional embodiments, various preferred media ingredients and cultivation conditions are described. These optional modes of carrying the process of this invention have been found to complement -- and thus still further improve --the yields and control imparted by the present fatty acids. The microorganisms useful in this process a.e the oil synthesizing yeasts. Many such yeasts which are naturally capable of oil synthesis are already known and available in the art. Particuiarly preferred, however, are species from the genus Rhodosporidium, Lipomyces, Candida, Endomyces, Saccharomyces, or Rhodotorula. Such yeasts are among those which are naturally higher accumulators of oils (or fats). These oil-synthesizing yeasts are well known and can be isolated by conventional processes from their native sources -such as leaves, vegetable stems or the like, as the case may be. More conveniently, however, they are available from the various culture storage depots (including, for example, the American Type Culture Collection in Maryland, U.S.A.). At such depots it is often possible to obtain even a variety of different cultures of a given yeast species. While any of the known oil-synthesizing yeasts may be employed in the process of the present invention, it is preferred to utilize those naturally inclined to the synthesis and storage of large amount of oils. Thus, for example, yeasts having the ability to accumulate at least 209 oil (more desirably at least 30%) on a standard culture medium such as a glucose, ammonium salt, and minerals medium are preferred. They are more susceptible to modification to desired levels of oil synthesis in accordance with the present process. Illustrative of the available oil-synthesizing yeasts are Rhodosporidium toruloides - MCC nos. 26194, 26217, 10657, 10788 and 32767 Liparroes z s starkeyii - MCC no. 12659 Liparoes z s lipoferus - MCC nos. 10742 and 32371 Candida revkaufi - ATCC. nos. 10570 and 18470 Candida pulcherrima - ATCC nos. 7696, 7697, 9889, 18406 and 22032 Candida tropicalis - MCC. nos. 750, 1369, 9968, 13803, 14056, 14246, 15114, 15543, 18213, 18526, 20005, 20006, 20007, 20115, 20175, 20215, 20240 and 20336 Candida utilis - ATOC nos. 8205, 8206, 9226, 9256, 9950, 15239, 16321, 20262 and 22023 Candida lipolytica - ATOC nos. 8661, 8662, 9773, 16617, 16618, 18942, 18943, 18944, 18945, 20114, 20182, 20237 and 20287 Saccharomyces cereuisae 500 types - ATOC nos. 11795 and 12341 are two examples Rhodotorula glutinis - MCC nos. 2527, 4054, 15125, 16725, 16726, 16740, 20147 and 20310 Ihodotorula graminis - MCC nos. 16727, 16728, 16729, 16730 and 18159 Trichosporon pullans - MCC nos. 9331 and 10677 Trichosporon cutaneum - ATOC nos. 757, 4155, 10267, 13445, 14254, 14255, 14905 and 22375 (It should be noted that the Trichosporon species were formerly known as Endaoes). The initial selection of a particular yeast species may -- to the extent known in the art -- suggest various bene ficial ingredients for g culture or fermentation medi . If so, such preference may be followed to the extent -- described in detail below -- that does not conflict with the present inven tion. In general, however, suitable media may be prepared from any of their common constituents, the only caveat being that a predominent carbon nutrient source must be composed of the fatty acids that control the end product of this invention. These media, of course, generally are dilute and of aqueous base. Their solid constituents -- predominently carbon and nitrogen nutrient sources -- ordinarily compose less than about 6t by total weight. In addition, media are ordinarily adjusted or buffered to within the pH range of between about 4.0 and 6.0. This is the optimum range for yeast cultivation. As a nitrogen nutrient source for the medium, organic materials such as asparagine, glutamine, peptones and the like are suitable. Alternatively, minerals such as ammonium salts or urea may be employed. Preferably, however, one of the common industrial waste materials ri:h in nitrogen is employed. Of these, cornsteep is particularly desirable. Cornsteep is the aqueous liquor formed in the conventional corn-wet-milling process when dry corn is soaked in warm, dilute sulfurous acid. While composed of about 258 by total weight of crude protein (8t nitrogen by dry weight), it also commonly contains small amounts of ash, sugars and other beneficial culture constituents. Although it may be augmented with additional nitrogen-containing materials, cornsteep alone represents an inexpensive, but essentially complete, nitrogen nutrient source. The culture medium also should include the known essential metabolic mineral salts, including potassium, sodium, calcium, magnesium, iron and the like, Further, such secondary nutrients as vitamins and amino acids are desirable, particularly where the cultivation period is intended to be extensive. Suitable carbon nutrient sources which may be present in the culture medium are the monosaccharides, disaccharides, oligosaccharides and polysaccharides such as starch hydrolyzates. Alternatively, various diverse sources including hydrocarbons or lower fatty acids including industrial wastes such as cheese production liquors, wood saccharificaton waste liquors and the like may be incorporated into the culture medium. Whether or not such other carbon nutrient sources are provided as a part of the culture medium1 however, the culture must contain a predominant amount of one or more fatty acids having between 10 and 20 carbons. This content of fatty acid is necessary because it also serves as the primary means of modi fying the oil-synthesis of the yeast cells. Furthermore, because the ability of the fatty acid(s) to act as a modifier of cellular oil synthesis may be partly masked by the presence of other carbon nutrient sources, it is preferred that such other sources be maintained at a level of less than 509 of total carbon source. Most preferably, the fatty acid source constitutes all or essen tially all of the available nutrient carbon in the culture medium. The fatty acid employed as the carbon source may be obtained from any number of known sources and/or be of a variety of compositions. Most simply, for example palmitic (C16:0), stearic rr (C18:0) ) or oleic (C18:i) fatty acid is generally avail- able commercially in either free acid or simple salt -- such as sodium salt -- form of high purity. These =are prevalent fatty acids are therefore readily employed either alone or as admix 4. tures. Polyunsaturated fatty acids -- especially linoleic (C18:2) and linolenic (C18:3) -- and other less common fatty acids having 16 to 20 carbons may also be obtained in pure form, but are available in greater and more inexpensive quantities in various known commercial admixtures such as soapstock, discussed below. Although the composition of the carbon source is of only minor concern as regards its nutrient function, that composition becomes of major importance in fulfilling the second function of the fatty acids -- viz., modificatlon and control over oilsynthesis occurring within the yeast cells. Here the specific fatty acid or admixture is particularly vital to preselection of the chemical composition of the product oil and also to the degree of increase from conventional oil yields. The importance of this fatty acid composition in the culture medium stems from the fact that each individual fatty acid causes a different kind of shift in the oil-synthesizing metabolism of a given yeast species. Moreover, the result of admixtures of fatty acids is a collective interaction which compounds -- but not necessarily in linear fashion -- these individual shifts. Hence, given product oils are chiefly produced through orchestration of a proper mix of fatty acids in the carbon source. In view of the complexity of their mode of modification of.oil-synthesis, accurate prediction of the precise yield and oil composition to be obtained from any given fatty acid carbon source must be at least partly empirically-based. This does not, however, present any serious impediment to the prac tice of this invention.. -Conventional analytical practices permit determination of the yield and composition of oil resultant from any particular culture. Hence routine experimentation will soon permit identification of'fatty acid carbon sources suitable for the production of any given oil. Furthermore, even the degree of experimentation involved may be reduced by the fact that certain general rules as to the effect of the fatty acids on oil-synthesis exist. For example, the presence of fatty acid of any given carbon length in the carbon source ordinarily results in an increase in the proportion of esters of that same length in the oil. Similarly, the degree of saturation/unsaturation (and particularly polyunsaturation) in product oil is directly related to the corresponding saturation level in the fatty acid coSposition of the carbo±: sugtce. As will become more evident from the further description and examples which follow, such general rules -- while helpful -- are incomplete. Variation in desired oil, yeast species, media constituents and cultivation conditions all exert some influence over oil production. Because, however, the major modifying effect derives from these carbon source fatty acids of from 10 to 20 carbon, it is relatively easy to approximate any desired kind of oil production. Further accuracy may thsr. be obtained through such secondary modifying factors so as to provide a complete set of the parameters necessary for preselected and optimal operation of a given, desired oil. Among the secondary factors discovered to affect oilsynthesis, tato are of particular importance. These factors relate to the state of the yeast cells themselves and to the conditions under which they are cultivated. The metabolic state of a yeast cell, for example, may be considered to be balanced between two major avenues. On the one hand, the cell may be in a growth stage in which production of protein etc. is the predominant activity. Alternatively, the cell may be relatively inert as to growth and instead concentrate upon synthesis and storage of fat. Obviously, however, the latter state of metabolic activity is more desirable where high yield of oil is sought. Fortunately, it has been discovered that the cellular state of a yeast depends upon the composition of the medium in which it is being cultivated. More specifically, for example, it is possible to favor the production of oil through the expedient of minimizing the amount of nitrogen nutrient source in the medium. Some nitrogen source -- the amount depending largely on the ye species being cultivated -- is'always necessary. However, by reducing its content to, for example, the range of between about .005 to 0.2% by nitrogen weight (as compared to the preferred range of 0.5 to 5.08 by carbon weight for the carbon source) further improvement in yield may be obtained. In a similar manner, the content of dissolved oxygen in the medium may affect the yeast cells directly. Whether or not such effect results from cellular oxidation of stored oil, aerobic cultivation of these yeasts at different levels of oxygen in the culture medium may substantially increase the final yield of recovered oil. In contrast to the above, the effects of the conditions of yeast cultivation are also reflected in the composition of the resultant oils. Here, temperature appears most significant. While desirable cultivation may ordinarily occur throughout the preferred range of from about 20 to O-C, it has been dis covered that from 30 to 400C favors the production of saturated oils, while at 20 to 30?C the oil synthesized is relatively more unsaturated in its fatty acid constituents. In addition to this compositional effect, however, some increase in yield with elevated temperatures is also common. Through use of the foregoing means for modifying oilsynthesis in yeast, various types of particularly useful and/or scarce oils may be produced. For example, an especially desirable product is an oil containing a substantial proportion of disaturated, unsaturated triglyceride. The value of, for example, cocoa butter lies largely in its content of such an oil (in which the unsaturated acid generally occupies the middle position). This invention thus offers a means of producing high yields of oils tailored to meet particular demands. For example a functional cocoa butter substitute can be produced through microbiological means. As has already been indicated, the fatty acid and optional modifying means of this invention readily permit control over the degree of saturation in product oils. The ratio of saturated-to-unsaturated acid constituents of in such glyceryl oils may readily controlled to achieve the approximate level of 2.0 thus approximating cocoa butter. Similarly, assurance of high contents of palmitic, oleic and stearic radicals (as normally are predominant in cocoa butter) is easily afforded by selection of a carbon source rich in these acids. Other valuable oils readily produced in accordance with the present invention are oils high in polyunsaturates. By selection of a carbon source which is itself rich in polyunsaturated acids, such an oil is readily produced. Use of such polyunsaturates readily permits production of oils having a polyunsaturated/saturated ratio of 2.0 or more. Moreover, for this purpose, one of the previously mentioned commercial admixtures such as soapstock (a waste product of vegetable oil refining which is particularly rich in linoleic and linolenic acids) may be utilized as all or a part of the fatty acid carbon source. This then substantially reduces the cost of ingredients utilized in the oil synthesis. Once the yeast cells have been cultivated for the desired period of time (ordinarily between from about 1 to 7, more desirably 2 to 5, days), the medium should be separated. This may be accomplished by any of the conventional means such as filtration or centrifugation. Additionally, improved separation may be afforded by washing with water or the like, as desired. After separation of the cells, their oil content is removed. Again, conventional means may be employed. Preferably, however, recovery follows a two-step pattern in which the cells are first subjected to rupture by, for example, frcezing or hydrolysis and then the oil is extracted from the cellular debris with 2. suitable (usually volatile, to facilitate subsequent removal) solvent. In a further embodiment, the cell debris may also be dried prior to extraction or during rupture, as with freeze-drying. This further improves the purity of the recovered oil. Further illustrative of the present invention are the examples which follow. In the examples, all proportions are on a weight basis unless otherwise indicated. EXAMPLE 1 Ten culture flasks were filled with growth media containing 1.0% cornsteep and. 2.0% sodium salt compositions of various fatty acids. The acids of these salts were as follows: Media/Flask Fatty Acid Composition 1 2.0% palmitic (i.e., sodium palmitate) 2 2.0% stearic (i.e., sodium stearatc) 3 2.0% oleic (i.e., sodium oleate) 4 .66% palmitic; .668 stearic; .668 oleic 5 1.0% palmitic; 1.0% stearic 6 1.0t stearic; 1.0% oleic 7 1.0t palmitic; 1.08 oleic B 1.338 palmitic; .33% stearic; .33% oleic 9 .33t palmitic; 1.33% stearic; .33% oleic 10 .33% palmitic; .33% stearic; 1.33X olcic Each of the media was adjusted to a pH of 5.0. inoculated with Rhodosporidium torulodies (ATCC 10788). placed in an aerated shake incubator, and there maintaired at 270C under agitation for 7 days. The yeast cells were then harvested by centrifugation washed with cold, sterile water dried by rccentrifugation and the cells were frozen until their oil content could be analyzed. Sample No. 1 2 3 4 5 6 7 8 9 10 Lipid Content (%) 66 60 47 66 67 65 72 79 70 67 Fatty Acids C 14:0 1.3 1.7 1.5 1.5 1.1 1.6 1.9 1.9 1.8 1.7 C 16:0 62.5 39.7 6.8 52.8 48.1 39.2 54.2 71.4 42.1 17.7 C 16:1 0.7 0.3 1.1 C 18:0 12.2 38.9 1.0 19.4 27.3 33.7 1.3 9.7 27.2 2.4 C 18:1 22.6 16.9 67.3 18.1 16.6 22.3 40.2 15.4 21.0 64.5 C 18:2 1.0 1.6 5.2 0.7 0.9 1.0 1.9 1.0 1.5 3.0 C 18: :3 1.0 0.2 0.3 0.6 0.6 Saturated 76 80 9 74 77 75 57 83 71 22 Monosaturated 23 18 67 18 17 23 40 15 21 65 Polyunsaturated 1 2 6 1 1 1 2 1 2 4 Unknown 0 0 18 7 5 1 1 1 6 9 Iodine Value 21.2 17.8 69.6 17.3 16.1 22.6 37.8 15.0 22.7 62.2 The yields of oil (provided on the basis of percent by total dry cell weight) from the different media are depicted graphically in FIG 1 othe drawings. Tlle three axes of the figure represent the relative amounts of palmitic, stearic and oleic acids in the 2.0% fatty acid fraction of the growth medium. There the effect of the differing fatty acid carbon sources or modifying agents are seen to be considerable. The weight percent of oil in the cultivated cells varies from less than 45% to more than 70t by weight, dependent solely upon the composition of the fatty acids present in the media. In FIG 2, the effete of the different carbon sources upon the composition of the oil itself is. depicted. This graph charts the changes in the composition of the yeast lipid as measured by the ratio of saturated-to-unsaturated fatty acid constituents thereof as a function of the substrate composition on which the yeast is grown. Again the effect is considerable. Moreover, the graphed results depend solely upon the degree of saturation/unsaturation of the tatty acids of the media carbon sources showing that the individual fatty acid directly influence the nature of the metabolic functions of the yeast cells. EXAMPLE 2 A set of 3 liter samples of 4 different media were inoculated to a 2% level with Rhodosporidium torulodies (ATCC 10788). The set contained a control media of 1.0% cornsteep and 2.0% soapstock. The remaining 3 samples in the set contained 1.09 cornstcep, 1.59 soapstock and 0.58 of one of palmitic acid, stearic acid and oleic acid, respectively. All samples were incubated for 3 days under aeration and agitation at 250C. The yeast cells were then treated as in Example 1 for recovery of their oil content. The analyses of the oil contents of these samples are depicted below in conjunction with the corresponding fatty acid carbon sources of the various media. This data underlines the complexity of action of the fatty acid carbon sources. Illustrative is the divergence in effect between the oleic (%4) and plamitic (42) enriched sources versus the stearic (µ3) enriched one. Modification of.oil composition of the former class proceeds with large increases in the presence of the enhancing fatty acid as compared to the control of soapstock (%1). With stearic ac'd, however, the oil synthesized shows a much smaller increase in that acid which may be due to metabolization of that acid or a feedback inhibition mechanism. Media Composition Oil Composition (3 day culture) Fatty Acids &num;1 &num;2 &num;3 &num;4 &num;1 &num;2 &num;3 &num;4 (16:0) (18:0) (18:1) (16:0) (18:0) (18:1) C 14:0 0.1 0.1 0.1 0.1 0.3 0.9 1.2 0.6 16:0 17.4 37.9 12.9 12.9 14.0 38.7 31.8 31.8 16:1 0.2 0.2 0.2 0.2 0.7 -- 2.2 8.9 18:0 4.6 3.3 26.3 3.3 0.8 0.2 9.8 - 18:1 24.0 18.0 18.0 43.0 31.8 24.6 39.0 53.2 18:2 22.5 16.8 16.8 16.8 44.4 30.0 12.1 21.8 18:3 26.2 19.6 19.6 19.6 7.0 4.9 -- 2.1 Saturated 22.1 41.3 41.3 16.3 15.1 39.8 43.6 14.0 Monosaturated 24.2 18.2 18.2 43.2 32.5 24.6 41.2 62.1 Polyunsaturated 48.7 36.4 36.4 36.4 51.4 34.9 12.1 23.9 EXAMPLE 3 Four culture flasks containing growth media having a soapstock/cornsteep base were prepared. These media differed only in the ratio of these two constituents. The flasks were inoculated with Lipomyces starkevi to a 29 level and cultivated for 7 days as in Example 1. Analysis of the oil recovered from the yeast showed the following: Sample (Cornsteep/soapstock) (0.5%/2.5%) (1.3%/1.7%) (2.1%/0.9%) (2.5%/0.5%) Lipid Content 31.3t 51.8% 67.3% 39.1% Cell growth per ml* 3.4x107 2.6x107 2.1x107 1.6x107 Fatty Acids C 14:0 0.2 0.1 0.1 0.2 C 16:0 21.1 19.6 l9.8 21.1 C 16:1 0.4 0.2 0.4 0.6 C 18:0 4.7 4.3 2.6 1.9 C 18:1 12.4 13.8 24.2 29.7 C 18:2 52.2 53.8 36.4 31.5 C 18: :3 7.2 6.4 14.8 13.9 Polyunsaturated 59.4t 60.2t 51.2% 45.4t Monounsaturated 12.8% 14.0% 24.6t 30.3% Saturated 26.1% 24.6% 22.8* 23.5% *as determined by Petroff-Hauser method The table shows the strong influence of variation in the amount of fatty acid carbon source or modifying agent present in the culture medium. This is particularly true with regard to the fatty acid profile of the glyceryl esters themselves. The differing oil-yield and cellular-growth values reflect the composite result of two factors. While higher concentrations of carbon source tend to stimulate production of oil per se, significant amounts of the nitrogen-rich cornsteep can cause a shift in cellular metabolism toward cell growth and away from oil production. This shift is reflected in the subsequent decline in yield. EXAMPLE 4 Candida utilis was cultivated in two media differing by the presence of cornsteep and soapstock in amount of 0.5%/2.58 and 2.5t/0.5% by weight, respcctively, Culture and recovery were as set forth in Example 3 except that a 7 day growth period was employed. The results were similar to those obtained in Example 3. At the higher level of fatty acid carbon source, the yield of oil was 58.2% with a corresponding growth factor of 1.2x108/ml. With the higher ratio of nitrogen-containing cornsteep. however, the growth factor increased to 1.5S108/ml and oil production declined to 37.78. Thus the desirability of controlling growth so as to favor oil production is again emphasized. EXAMPLE 5 Two growth media were prepared which differed only in their contents of cornsteep and soapstock. The first contained 0.5t cornsteep and 2.58 soapstock; the second, 0.9% and 2.1!, respectively. Yeast of the species Saccharomyces cerevisiae was grown and harvested after 7 days as in Example 4. Analysis of the recovered oils showed the following differences in major constituents. Culture Medium (cornsteep/soapstock) 0.5%/2.5% 0.9%/2.1% Fatty Acids C 16:0 13.9t 22.1t C 18:0 1.8% 3.0% C 18:1 13.7% 17.4% C 18:2 59.2t 49.7t Polyunsaturated 66.7% 53.9% Monounsaturated 14.8% 18.4% Saturated 15.9% 25.78 EXAMPLE 6 Rhodosporidium torulodies (ATCC 10788) was cultured in two media containing 2.0% soapstock fcr 7 days. The first sample, however, was cultivated at 250C and the second at 35-C. After recovery of the synthesized oil, analysis showed the following significant differences: Cultivation Temperature 27eC 37*C Lipid Content 53.3% 64.28 Fatty Acid Composition: C 16:0 27.4% 29.4% C 18:0 5.1% 5.1% C 18:1 11.2% 9.7% C 18:2 50.0% 48.6% C 18:3 3.5% 3.6% Saturated 34.0 35.4 Monounsaturated 12.0 11.0 Polyunsatured 53.5 52.2 Unknown 0.5 1.4 This illustrates the effect of tempera'are upon tho yield in synthesized oil. EXAMPLE 7 Two 3 1 samples of a 2.08 soapstock and 1.0% cornsteep medium were adjusted to a pH of 4.5 and inoculated with R. torulodies (ATCC 10788). Cultivation was then performed at 250C for 72 hours, with the distinction that in one sample the oxygen level was maintained at 30% of saturation while in the other, it was maintained at 80%. After recovery of tiie synthesized oil, analysis showed the following significant differences: 80% O2 30%O2 Lipid Content 39.4% 47.4% Oil Composition C 16:0 10.1% 12.48 C 18:0 1.7% 1.9% C 18:1 15.5% 14.5% C 18:2 66.7% 63.7% C 18:3 5.5t 5.3 The available oxygen content is thus seen to have a major effect on the yield of oil and a minor one on the degree of saturation, particularly polyunsaturation, of the product oil.

Claims: Claims 1. A process for the microbiological production of oil comprising aerobically cultivating oil-synthesizing yeast cells in a culture medium in which the carbon nutrient source consists essentially of fatty acid having between 10 and 20 carbons, separating the cultivated cells from said medium and recovering the intracellular oil of said cells. 2. The process according to Claim 1, wherein the fatty acid carbon source is between 0.5 and 5.0 % carbon by weight of medium. 3. The e process according to any of the preceding claims, wherein the medium contains a nitrogen source of between .005 and 0.2 % nitrogen by weight of medium. 4. The process according to any of the preceding claims, wherein the oil-synthesizing yeast is a species selected from the genus Rhodosporidium, Lipomyces, Candida, z ccharomyces, Endomyces or Rhodotorula. 5. The process according to any of the preceding claims, wherein the medium has a pH between 4.0 and 6.0 and cultivation is conducted at between 20 and 40 C. 6. The e process according to any of the preceding claims, wherein the carbon source coMprises soapstock. 7. The process according to any of the preceding claims, wherein the medium contains a nitrogen source comprising cornsteep. 8. The process according to any of the preceding claims comprising aerobically cultivating oil-synthesizing yeast cell in a culture medium, separating the cultivated cells fran said medium and recovering the intracellular oil fran said cells, whereby said medium contains a carbon nutrient source selected fran the group consisting of fatty acid having fran 10 to 20 carbons, said source being present in an amount sufficient to modify cellular oil synthesis to produce a recoverable glyceryl-ester oil with a fatty acid saturated/unsaturated ratio in the range fran about 0.5 to 4.5 and total yield of at least 50 % oil by dry cell weight. 9. The process according to any of the preceding claims comprising (a) preparing a growth mcdium in which the carbon nutrient source comprises fatty acids having between 10 and 20 carbons, (b) inoculating the growth medium with oil synthesizing yeast cells, (c) aerobWcally cultivating the yeast eElls; (d) separating the cultivated cells from the medium, and (e) recovering oil from the cultivated cells, wherein the composition of the oil synthesized is dependent upon the ratio of saturated fatty acid to unsaturated fatty acid in the medium. 10. The process according to any of the preceding claims, wherein the growth medium is enriched with a fatty acid selected fran the group consisting of palmetic acid, stearic acid, oleic acid and combinations thereof. 11. The process of Claim 10 wherein the fatty acid component is the growth medium is comprised predaninately of soapstock. 12. The process according to any of the preceding claims wherein the cultivated cells yield at least 50 % oil by dry cell weight.

Inventors: PICATAGGIO, STEPHEN K., SMITTLE, RICHARD B.
Applicants: CPC INTERNATIONAL INC.
Application year: 1979
Main classification: C12P7
IPC codes: C12R1, C12N1, C12P7