US3264196A - Purification of micro-organisms cultivated on hydrocarbon feedstock - Google Patents

Purification of micro-organisms cultivated on hydrocarbon feedstock Download PDF

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US3264196A
US3264196A US330527A US33052763A US3264196A US 3264196 A US3264196 A US 3264196A US 330527 A US330527 A US 330527A US 33052763 A US33052763 A US 33052763A US 3264196 A US3264196 A US 3264196A
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organism
hydrocarbon
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Filosa Jean Antoine
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    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/26—Processes using, or culture media containing, hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P21/00—Preparation of peptides or proteins
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00—Chemistry: molecular biology and microbiology
    • Y10S435/8215—Microorganisms
    • Y10S435/911—Microorganisms using fungi
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00—Chemistry: molecular biology and microbiology
    • Y10S435/8215—Microorganisms
    • Y10S435/911—Microorganisms using fungi
    • Y10S435/921—Candida
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00—Chemistry: molecular biology and microbiology
    • Y10S435/8215—Microorganisms
    • Y10S435/911—Microorganisms using fungi
    • Y10S435/921—Candida
    • Y10S435/923—Candida lipolytica
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S435/00—Chemistry: molecular biology and microbiology
    • Y10S435/8215—Microorganisms
    • Y10S435/911—Microorganisms using fungi
    • Y10S435/944—Torulopsis

Definitions

  • micro-organism In a process in which a micro-organism is cultivated in the presence of a hydrocarbon it has now been found that the micro-organism may be contaminated by absorbed. hydrocarbons. Sometimes other materials formed in the fermentation process may be present, thus yeasts may be contaminated by lipids.
  • the purification stage may be employed to eliminate lipids, esters, ketones and/or free fatty acids, or to reduce their quantity in association with amicro-organism, for example, a yeast.
  • the hydrocarbon feedstock contains C or higher.
  • a hydrocarbon fraction derived from petroleum is preferred.
  • a process which comprises cultivating a micro-organism in the manner as hereinbefore described in the presence of a petroleum fraction consisting in part of straight chain hydrocarbons and having a mean molecular weight corresponding to at least 10 carbon atoms per molecule, and in the presence of an aqueous nutrient medium; and in the presence of a gas containing free oxygen and separating from the mixture, on the one hand, the micro-organism and, on the other hand, a petroleum fraction having a reduced proportion of straight chain hydrocarbons or which is free of said straight chain hydrocarbons.
  • the process of the invention is of particular value for the treatment of petroleum gas oil fractions which contain straight chain hydrocarbons in the form of waxes, since by the process of the invention, a gas oil of improved pour point is obtained while the waxes are converted to a valuable product.
  • straight-chain hydrocarbons will be present in the feedstocks according to the invention as parafiins; however, the straight chain hydrocarbons may be present as olefins; also there may be used a mixture containing straight chain paraffins and olefins.
  • the percentage conversion of straight chain hydrocarbons which is achieved can be maintained at a value approaching without necessitating a very disproportionate expenditure of contact time to achieve small improvements. Furthermore, in the continuous: process, this high percentage conversion can be achieved without resorting to the use of a long reaction path.
  • Micro-organisms which are cultivated as herein described may be yeasts, moulds or bacteria.
  • a yeast is employed this is of the family Cryptococcaceae and particularly of the subfamily Cryptococcoideae; however, if desired there may be used, for example, ascosporogeneous yeasts of the sub-family Saccharomycoideae.
  • Preferred genera of the Cryptococcoideae sub-family are Torulopsis (also known as Torula) and Candida.
  • Preferred strains of yeast are as follows. In particular it is preferred to use the specific stock of indicated reference; these reference numbers refer to CBS stock held by the Central Bureau vor Schimmelculture, Baarn, Holland, and to INRA stock 3 held by the Institut National de la Recherche Agrono- Inique, Paris, France.
  • Suitable moulds are of the family Aspergillaceae.
  • a suitable genus is Penicillium.
  • Penicilliam expansum Preferably there is used Penicilliam expansum.
  • Another suitable genus is Aspergillus.
  • cultivation is carried out in the presence of an aqueous nutrient medium.
  • an aqueous nutrient medium may be employed.
  • certain solid nutrient media may be employed.
  • Penicillium expansum is suitable for cultivation in an aqueous nutrient medium containing hydrocarbons.
  • Penicilliwm roqaeforti, Penicilliam notatum, Aspergillas fussiga tas and Aspergillus niger, Aspergillas versicolor may be used for cultivation on a solid agent containing hydrocarbons as feedstock.
  • the bacteria which are employed are of the family Bacillaceae and Pseudomonad-aceae.
  • Preferred species are Bacillus megateriam, Bacillus subtilis and Pseadomonas aeruginosa.
  • Other strains which may be employed include:
  • a typical nutrient medium for the growth of Nocardia a genus in the Actinomycetales order, has the following composition:
  • a suitable nutrient medium for yeast (and moulds) has the composition:
  • the growth of the micro-organism used is favoured by the addition to the culture medium of a very small proportion of extract of yeast (an industrial product rich in vitamins of group B obtained by the hydrolysis of a yeast) or more generally of vitamins of group B and/or biotin.
  • This quantity is preferably of the order of 25 parts per million with reference to the aqueous fermentation medium. It can be higher or lower according to the conditions chosen for the growth.
  • the growth of the micro-organism takes place at the expense of the feedstock fraction with the intermediate production of bodies having an acid function, principally fatty acids, in such manner that the pH of the aqueous mineral medium progressively diminishes. If one does not correct it the growth is fairly rapidly arrested and the concentration of the micro-organism in the medium, that is cellular density, no longer increases so that there is reached a so-called stationary phase.
  • the aqueous nutrient medium is maintained at a desired pH by the step-wise or continuous addition of an aqueous medium of high pH value.
  • an aqueous medium of high pH value usually, when using moulds or yeasts and in particular when using Candida lipolytica, the pH of the nutrient medium will be maintained in the range 36 and preferably in the range 4-5. (Bacteria require a higher pH, usually 6.5-8.)
  • Suitable alkaline materials for addition to the growth mixture include sodium hydroxide, potassium hydroxide, disodium hydrogen phosphate and ammonia, either free or in aqueous solution.
  • the optimum temperature of the growth mixture will vary according to the type of micro-organism employed and will usually lie in the range 25-35 C. When using vC'zagugda lipolytica the preferred temperature range is 28-.
  • the take-up of oxygen is essential for the growth of the micro-organism.
  • the oxygen will usually be provided as air.
  • the air used to provide oxygen, should be present in the form of fine bubbles under the action of stirring.
  • the air may be introduced through a sintered surface. However there may be used the system of intimate aeration known as vortex aeration.
  • the micro-organism will usually grow initially at a low rate of increase in cellular density. (This period of growth is referred to as the lag phase),
  • the rate of growth will increase to a higher rate of growth; the period at the higher rate of growth is referred to as the exponential phase and subsequently again the cellular density will become constant (the stationary phase).
  • a supply of the micro-organism for starting the next batch will preferably be removed before the termination of the exponential phase.
  • the growth operation will usually be discontinued before the stationary phase.
  • micro-organism will usually be separated from the bulk of the un-used feedstock fraction.
  • the major part of the continuous aqueous phase is first separated; preferably this is carried out by centrifuging, or decanting.
  • the separated aqueous phase will usually contain a greater concentration of non-nutritive ions than can be tolerated in the recycle stream and when this is so, only a proportion of the recovered aqueous phase can be recycled.
  • the recycle stream is supplied with make-up quantities of the necessary nutrients and is returned to the fermenter; if desired the make-up materials may 'be fed to the fermenter as a separate stream.
  • a micro-organism cream consisting of microorganism, having a quantity of oil fixed onto the cells, together with aqueous phase.
  • Fraction (iii) will then be mixed with an aqueous nutrient medium, which may be the same as or different from the aqueous nutrient medium employed in the growth stage, and is maintained in admixture with a gas containing free oxygen whereby the hydrocarbon contaminating the micro-organism is reduced in quantity or is eliminated.
  • an aqueous nutrient medium which may be the same as or different from the aqueous nutrient medium employed in the growth stage, and is maintained in admixture with a gas containing free oxygen whereby the hydrocarbon contaminating the micro-organism is reduced in quantity or is eliminated.
  • the major part of the continuous aqueous phase is separated with recycle of a proportion of the recovered aqueous phase, as hereinbefore described; recycle may be to either the growth stage or purification stage as desired.
  • this cream may be further treated for the removal of traces of oil which may be held to the cells.
  • the micro-organism cream may be washed with an aqueous solution of a surfactant and thereafter with water.
  • yeast may be dried under conditions suitable for its subsequent use as a foodstuff.
  • the product obtained at the end of the growth stage may be maintained without the addition of feedstock but with continued mixing (in a purification stage) with a gas containing free oxygen, whereby contaminants in the micro-organism are reduced in quantity or are eliminated.
  • the micro-organism may be recovered after the purification stage as hereinbefore described.
  • the process may be operated continuously or batchwise.
  • stages of the process may be carried out entirely batchwise. However, if desired, any one or more stages herein described may be carried out in continuous manner.
  • cellular density is expressed as dry Weight of yeast per litre of culture.
  • Example 1 4-0 litres of an aqueous mineral nutrient medium having the composition given below were introduced in a stainless steel fermenter having an effective capacity of 60 litres.
  • the aqueous nutrient medium had the composition:
  • the temperature of the culture was kept at 30:1" (1., pH at 4 and aeration and agitation giving 3 millimoles of 0 per litre of medium per minute. 10 N ammonia was admitted by an automatic pH controller.
  • the yeasts were recovered at 25 hours and at 40 hours by centrifuging and washing at +5 C. They were then dried by lyophilisation and analysed. Their total lipid content (fraction soluble in hexane) was 18% when recovered after 25 hours and 3% when. recovered after 40 hours.
  • Example 2 A similar experiment was carried out to that described in Example 1 except that the yeast was recovered from the culture liquor at 25 hours and then placed in 60 litres of fresh mineral medium, without hydrocarbon, in the same fermenter. The mixture was then stirred 10 hours under the same culture conditions (temperature 30 C. pH aeration 3 millimoles 0 per litre per hour). The cellular density was of the order of 15 grams/litre at the start, and remained constant throughout the process. Even though the 'yeast contained dry 20% weight of total lipids at the moment of introduction into the new medium, after the starvation treatment it did not contain more than 8% by wt.
  • Example 3 A similar experiment to that described in Examples 1 and 2 was carried out on yeasts from continuous fermentation, but in this case it was necessary to work with washed yeasts in a fresh medium, as in the continuous process one cannot obtain a racking-01f liquor entirely free of assimilable carbon substrate.
  • the culture in the 60 litre fermenter was stabilised at 0.1 litre/hour of total mineral medium plus gas-oil per litre of culture in the fermenter.
  • the operating conditions having been fixed (in particular temperature at 30 C. and pH at 4), the yeast was removed from part of the culture by centrifugation at +5 C. After washing it was put into a 20 litre fermenter containing 15 litres of the mineral medium given in Example 1, to give a cellular density of 20 grams/ litre.
  • the pH was regulated automatically to 4, the temperature to 30 C. and the air fiow and agitation so as to give 3 millimoles of oxygen per litre of culture per minute.
  • the treatment was applied for hours.
  • the cellular density remained 20 grams/litre throughout the experiment.
  • the yeasts were analysed for their fat content at the beginning and end of the process. A marked fall in fat content was observed, from to 5% by wt. on dry matter.
  • a process which comprises, in a growth stage, cultivating a straight chain hydrocarbon consuming microorganism in the presence of a hydrocarbon feedstock comprising at least in part straight chain hydrocarbons; in the presence of an aqueous nutrient medium; and in p the presence of a gas containing free oxygen and subsequently recovering a micro-organism free of a substantial amount of hydrocarbon but containing a small amount of hydrocarbon as contaminant, and thereafter in a puri- 'fication stage are carried out in separate fermentation zones.
  • a processing according to claim 1 in which the micro-organism which is cultivated is a yeast.
  • yeast is Candida lipolytica.
  • microorganism is a "bacteria.
  • a process according to claim 1 wherein in the process of recovering the micro-organism free of a substantial amount of hydrocarbon it is necessary to separate the micro-organism from the bulk of unconsurned hydrocarbon.

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Description

United States Patent 3,264,196 PURIFICATION OF MICRO-ORGANISMS CULTI- VATED 0N HYDROCARBGN FEEDSTOCK Jean Antoine Filosa, Lavera, France, assignor to The British Petroleum Company Limited of Britannic House, London, England, a British joint-stock corporation No Drawing. Filed Dec. 16, 1963, Ser. No. 330,527 Claims priority, application Great Britain, Dec. 31, 1962, 49,057/62 13 Claims. (Cl. 195-32) This invention relates to a process for the production of micro-organisms, for example, yeasts. This invention also relates to a process for the removal of straight chain hydrocarbons, wholly or in part, from mixtures of said hydrocarbons with other hydrocarbons.
In a process in which a micro-organism is cultivated in the presence of a hydrocarbon it has now been found that the micro-organism may be contaminated by absorbed. hydrocarbons. Sometimes other materials formed in the fermentation process may be present, thus yeasts may be contaminated by lipids.
It has also now been found that under certain conditions these contaminants or part thereof will constitute a feedstock for the micro-organism whereby the quantity of said contaminants may be reduced.
In accordance with the present invention there is provided a process which comprises, in a growth stage, cultivating a micro-organism in the presence of a hydrocarbon feedstock consisting wholly or in part of straight chain hydrocarbons; in the presence of an aqueous nutrient medium; and in the presence of a gas containing free oxygen and subsequently, if necessary, separating the micro-organism from the bulk of the unconsumed hydrocarbon whereby there is obtained a microorganism free of a substantial amount of hydrocarbon but containing a small amount of hydrocarbon as contaminant, and thereafter in a purification stage maintaining said micro organism with an aqueous nutrient medium and a gas containing free oxygen, whereby the hydrocarbon contaminating the micro-organism is reduced in quantity or is eliminated.
Alternatively or additionally the purification stage may be employed to eliminate lipids, esters, ketones and/or free fatty acids, or to reduce their quantity in association with amicro-organism, for example, a yeast.
Preferably the hydrocarbon feedstock contains C or higher. Suitably there may be used a hydrocarbon fraction derived from petroleum.
It is well-known that certain petroleum fractions, particularly gas oils, contain straight chain hydrocarbons, mainly paralfins which are waxes and which have an adverse effect upon the pour point of the fraction; that is to say, when these hydrocarbons are removed, Wholly or in part, the pour point of the fraction is lowered. Usually the wax is removed by precipitation by means of solvents, the wax originally present in the fraction being recovered as such, that is, without conversion to more valuable products.
The petroleum fractions boiling below the gas oils, for example, heavy naphthenes and kerosines also contain straight chain hydrocarbons which are potentially valuable for conversion to other products but hitherto, in general, utilisation of these hydrocarbons has been rendered difficult by the necessity of recovering these hydrocarbons from the petroleum fractions, in which they are contained, before they can be converted to other products. According to a preferred feature of this invention 3,Zfil,l% Patented August 2, 1956 "Ice there is provided a process which comprises cultivating a micro-organism in the manner as hereinbefore described in the presence of a petroleum fraction consisting in part of straight chain hydrocarbons and having a mean molecular weight corresponding to at least 10 carbon atoms per molecule, and in the presence of an aqueous nutrient medium; and in the presence of a gas containing free oxygen and separating from the mixture, on the one hand, the micro-organism and, on the other hand, a petroleum fraction having a reduced proportion of straight chain hydrocarbons or which is free of said straight chain hydrocarbons.
The process of the invention is of particular value for the treatment of petroleum gas oil fractions which contain straight chain hydrocarbons in the form of waxes, since by the process of the invention, a gas oil of improved pour point is obtained while the waxes are converted to a valuable product.
Usually the straight-chain hydrocarbons will be present in the feedstocks according to the invention as parafiins; however, the straight chain hydrocarbons may be present as olefins; also there may be used a mixture containing straight chain paraffins and olefins.
It is an important feature of this invention that when cultivating yeasts in the presence of the feedstocks hereinbefore described under conditions favouring the growth of the yeasts at the expense of the straight chain hydrocarbons, the other hydrocarbons, for example iso-paraffins, naphthenes and aromatics are not metabolised or, at most, the proportion which is metabolised is very small. Furthermore, unlike conventional chemical processes governed by the law of mass action, the rate of removal of straight chain hydrocarbons is not substantially reduced as the proportion of these hydrocarbons in the overall mixture of hydrocarbons decreases (except, of course, in the very final stages of removal). Thus, when desired, the percentage conversion of straight chain hydrocarbons which is achieved can be maintained at a value approaching without necessitating a very disproportionate expenditure of contact time to achieve small improvements. Furthermore, in the continuous: process, this high percentage conversion can be achieved without resorting to the use of a long reaction path.
By the application of this process under conditions which limit the metabolisation of the straight chain hydrocarbons it is possible to operate with the removal of only a desired proportion of these hydrocarbons.
Suitable feedstocks to the process of the invention include kerosine, gas oils and lubricating oils; these feedstocks may be unrefined or may have undergone some refinery treatment, but will usually be required to contain a proportion of straight chain hydrocarbons in order to fulfill the purpose of this invention. Suitably the petroleum fraction will contain 345% by weight of straight chain hydrocarbons.
Micro-organisms which are cultivated as herein described may be yeasts, moulds or bacteria.
Preferably when a yeast is employed this is of the family Cryptococcaceae and particularly of the subfamily Cryptococcoideae; however, if desired there may be used, for example, ascosporogeneous yeasts of the sub-family Saccharomycoideae. Preferred genera of the Cryptococcoideae sub-family are Torulopsis (also known as Torula) and Candida. Preferred strains of yeast are as follows. In particular it is preferred to use the specific stock of indicated reference; these reference numbers refer to CBS stock held by the Central Bureau vor Schimmelculture, Baarn, Holland, and to INRA stock 3 held by the Institut National de la Recherche Agrono- Inique, Paris, France.
Candida lipolytica Candida palcherrima, CBS 610 Candida utilis 5 Candida utilis, variati major, CBS 841 Candida tropicalis, CBS 2317 T oralopsis colliculosa, CBS 133 Hansenala anomala, CBS 110 Oidium lactis N eurospora sitophila Mycoderma cancoillote, INRA; STV 11.
Of the above Candida lipolytica is particularly preferred.
Suitable moulds are of the family Aspergillaceae. A suitable genus is Penicillium.
Preferably there is used Penicilliam expansum. Another suitable genus is Aspergillus.
Usually the cultivation is carried out in the presence of an aqueous nutrient medium. If desired, certain solid nutrient media may be employed.
In either case, a gas containing free oxygen must be provided. I
Penicillium expansum is suitable for cultivation in an aqueous nutrient medium containing hydrocarbons.
Penicilliwm roqaeforti, Penicilliam notatum, Aspergillas fussiga tas and Aspergillus niger, Aspergillas versicolor may be used for cultivation on a solid agent containing hydrocarbons as feedstock. 3O
Suitably the bacteria are of one of the orders: Pseudomonadales, Eubacteriales and Actinomycetales.
Preferably the bacteria which are employed are of the family Bacillaceae and Pseudomonad-aceae. Preferred species are Bacillus megateriam, Bacillus subtilis and Pseadomonas aeruginosa. Other strains which may be employed include:
Bacillus amylobacter Xanthomonas begoniae Pseadomonas na triegens Flavobacterium devorans Arthrobacter sp. Acetobacter sp.
Micrococcus sp. Actinomyces sp.
Corynebacteriurn sp. Agrobacterium sp.
Pseudomonas syringae Aplanobacter sp. 4* H For the growth of the micro-organism it will be necessary to provide, in addition to the feedstock, an aqueous nutrient medium and a supply of oxygen, preferably in the form of air.
A typical nutrient medium for the growth of Nocardia, a genus in the Actinomycetales order, has the following composition:
Grams Ammonium sulphate 1 Magnesium sulphate 0.20 Ferrous sulphate, 7H O 0.005 Manganese sulphate, 1H O 0.002 Monopotassium phosphate 2 Disodium phosphate 3 0 Calcium chloride 1 Sodium carbonate 0.1
Yeast extract 0.008 Distilled water (to make up to 1000 mls.).
For other bacteria a suitable nutrient medium has the composition:
Monopotassium phosphate grams 7 Magnesium sulphate, 7H O do 0.2 Sodium chloride do 0.1 Ammonium chloride do 2.5 Tap Water (trace elements) ml 100 Yeast extract grams 0.025 Made up to 1000 ml. with distilled water.
A suitable nutrient medium for yeast (and moulds) has the composition:
Diammonium phosphate grams 2 Potassium chloride do 1.15 Magnesium sulphate, 7H O do 0.65 Zinc sulphate do 0.17 Manganese sulphate, 1H O do 0.045 Ferrous sulphate, 7H O do 0.068 Tap water -ml 200 Yeast extract grams 0.025
Distilled water (to make up to 1000 mls.).
Micro-organisms, and in particular yeast, when first cultivated with the use of hydrocarbon fractions as feedstock sometimes grow with difficulty and it is sometimes necessary to use an inoculum of a micro-organism which has previously been adapted for growth on the hydrocarbon fraction which it is intended to use. Furthermore the micro-organism although cultivated in the presence of an aqueous mineral medium containing the appropriate nutrient elements may grow with difiiculty, because the hydrocarbon fraction does not contain the growth factors which exist in carbohydrate feedstocks, unless these growth factors are added.
The growth of the micro-organism used is favoured by the addition to the culture medium of a very small proportion of extract of yeast (an industrial product rich in vitamins of group B obtained by the hydrolysis of a yeast) or more generally of vitamins of group B and/or biotin. This quantity is preferably of the order of 25 parts per million with reference to the aqueous fermentation medium. It can be higher or lower according to the conditions chosen for the growth.
The growth of the micro-organism takes place at the expense of the feedstock fraction with the intermediate production of bodies having an acid function, principally fatty acids, in such manner that the pH of the aqueous mineral medium progressively diminishes. If one does not correct it the growth is fairly rapidly arrested and the concentration of the micro-organism in the medium, that is cellular density, no longer increases so that there is reached a so-called stationary phase.
Preferably therefore the aqueous nutrient medium is maintained at a desired pH by the step-wise or continuous addition of an aqueous medium of high pH value. Usually, when using moulds or yeasts and in particular when using Candida lipolytica, the pH of the nutrient medium will be maintained in the range 36 and preferably in the range 4-5. (Bacteria require a higher pH, usually 6.5-8.) Suitable alkaline materials for addition to the growth mixture include sodium hydroxide, potassium hydroxide, disodium hydrogen phosphate and ammonia, either free or in aqueous solution.
The optimum temperature of the growth mixture will vary according to the type of micro-organism employed and will usually lie in the range 25-35 C. When using vC'zagugda lipolytica the preferred temperature range is 28- The take-up of oxygen is essential for the growth of the micro-organism. The oxygen will usually be provided as air. In order to maintain a rapid rate of growth the air, used to provide oxygen, should be present in the form of fine bubbles under the action of stirring. The air may be introduced through a sintered surface. However there may be used the system of intimate aeration known as vortex aeration.
It has been found that by the use of yeast of the strain Candida lipolytica in a process according to the invention in which aeration is effected by vortex aeration, a high growth rate is achieved whereby the generation time lies in the range 2-5 hours and the cell concentration is increased by a factor of up to 12 in two days.
In batch operation, the micro-organism will usually grow initially at a low rate of increase in cellular density. (This period of growth is referred to as the lag phase),
Subsequently the rate of growth will increase to a higher rate of growth; the period at the higher rate of growth is referred to as the exponential phase and subsequently again the cellular density will become constant (the stationary phase).
A supply of the micro-organism for starting the next batch will preferably be removed before the termination of the exponential phase.
The growth operation will usually be discontinued before the stationary phase.
At this stage the micro-organism will usually be separated from the bulk of the un-used feedstock fraction.
According to one method of treating the product the major part of the continuous aqueous phase is first separated; preferably this is carried out by centrifuging, or decanting. The separated aqueous phase will usually contain a greater concentration of non-nutritive ions than can be tolerated in the recycle stream and when this is so, only a proportion of the recovered aqueous phase can be recycled. Thus it will usually be possible to separate ca. 96% by wt. of the aqueous phase which is present in the product, of which on the same percentage basis, ca. 20% by wt. will be discarded. The recycle stream is supplied with make-up quantities of the necessary nutrients and is returned to the fermenter; if desired the make-up materials may 'be fed to the fermenter as a separate stream.
By centrifuging the product from the fermenter (preferably after decanting as described) three fractions are recovered. These are in order of increasing density:
(i) An oil phase containing micro-organism cells,
(ii) An aqueous phase containing traces of oil and micro-organism, and
(iii) A micro-organism cream consisting of microorganism, having a quantity of oil fixed onto the cells, together with aqueous phase.
Fraction (iii) will then be mixed with an aqueous nutrient medium, which may be the same as or different from the aqueous nutrient medium employed in the growth stage, and is maintained in admixture with a gas containing free oxygen whereby the hydrocarbon contaminating the micro-organism is reduced in quantity or is eliminated.
Again, preferably, the major part of the continuous aqueous phase is separated with recycle of a proportion of the recovered aqueous phase, as hereinbefore described; recycle may be to either the growth stage or purification stage as desired.
By centrifuging the product from the fermenter (preferably after separating the major part of the aqueous phase by decanting), there are obtained (i) An aqueous phase containing traces of microorganism.
-(ii) A micro-organism cream.
If necessary this cream may be further treated for the removal of traces of oil which may be held to the cells. To this end, the micro-organism cream may be washed with an aqueous solution of a surfactant and thereafter with water.
Finally the yeast may be dried under conditions suitable for its subsequent use as a foodstuff.
If desired the product obtained at the end of the growth stage may be maintained without the addition of feedstock but with continued mixing (in a purification stage) with a gas containing free oxygen, whereby contaminants in the micro-organism are reduced in quantity or are eliminated. The micro-organism may be recovered after the purification stage as hereinbefore described.
The process may be operated continuously or batchwise.
When operating continuously it will usually be necessary to provide separate fermenters or separate zones in the same fcrmenterfor the operation of the growth and purification stages.
Other steps which may be taken to obtain a purified micro-organism or a product derived therefrom or to improve the process in respect of the production of the unrrretabolised hydrocarbon fraction are described in the following applications; the use of any process herein described lies Within the scope of the present invention.
The stages of the process may be carried out entirely batchwise. However, if desired, any one or more stages herein described may be carried out in continuous manner.
The invention is illustrated but not limited with reference to the following examples.
Throughout these examples cellular density is expressed as dry Weight of yeast per litre of culture.
Example 1 4-0 litres of an aqueous mineral nutrient medium having the composition given below were introduced in a stainless steel fermenter having an effective capacity of 60 litres.
In order to keep the temperature in the fermenter constant at 30 0., water was circulated in an annulus constituted by the space between two concentrical cylinders, the smaller one being the fermenter itself.
The aqueous nutrient medium had the composition:
Grams Diammonium phosphate 2 Potassium chloride 1.15 Magnesium sulphate, 7H O 0.65 Zinc sulphate 0.17 Manganese sulphate, 1H O 0.045 Ferrous sulphate, 71-1 0 0.068 Yeast extract 0.025 Tap water 200 Distilled water add. 1000 ml.
20 litres of a 24 hour inoculum of Candida: lipolyfica on mixed C9-C16 normal hydrocarbons were then added, such that the cellular density was about 1 g. of dry matter per litre.
1.03 litres of heavy gas-oil, that is 15 grams/litre, were then added, this quantity being suflicient to take the cellular density to 2 grams/ litre.
The temperature of the culture was kept at 30:1" (1., pH at 4 and aeration and agitation giving 3 millimoles of 0 per litre of medium per minute. 10 N ammonia was admitted by an automatic pH controller.
When the flow of ammonia reached 20 ml. the addition of gas-oil was begun assuming a yield on gasoil of dry yeast produced gas-oil feed of 10% by weight and a cell division time of 3 hours. This addition was carried out every hour until 200 grams/litre, i.e. 13.8 litres had been added.
Starting with a cellular density of 2 grams/litre at 25 hours at the end of the exponential growth phase, a density of 15 grams/litre was obtained. This value remained constant during the stationary phase from 25 to 40 hours. During this period the yeasts were lacking in carbon feedstock, other elements being present in excess. It acted as a phase of starvation.
The yeasts were recovered at 25 hours and at 40 hours by centrifuging and washing at +5 C. They were then dried by lyophilisation and analysed. Their total lipid content (fraction soluble in hexane) was 18% when recovered after 25 hours and 3% when. recovered after 40 hours.
Example 2 A similar experiment was carried out to that described in Example 1 except that the yeast was recovered from the culture liquor at 25 hours and then placed in 60 litres of fresh mineral medium, without hydrocarbon, in the same fermenter. The mixture was then stirred 10 hours under the same culture conditions (temperature 30 C. pH aeration 3 millimoles 0 per litre per hour). The cellular density was of the order of 15 grams/litre at the start, and remained constant throughout the process. Even though the 'yeast contained dry 20% weight of total lipids at the moment of introduction into the new medium, after the starvation treatment it did not contain more than 8% by wt.
Example 3 A similar experiment to that described in Examples 1 and 2 was carried out on yeasts from continuous fermentation, but in this case it was necessary to work with washed yeasts in a fresh medium, as in the continuous process one cannot obtain a racking-01f liquor entirely free of assimilable carbon substrate.
The culture in the 60 litre fermenter was stabilised at 0.1 litre/hour of total mineral medium plus gas-oil per litre of culture in the fermenter.
The operating conditions having been fixed (in particular temperature at 30 C. and pH at 4), the yeast was removed from part of the culture by centrifugation at +5 C. After washing it was put into a 20 litre fermenter containing 15 litres of the mineral medium given in Example 1, to give a cellular density of 20 grams/ litre.
The pH was regulated automatically to 4, the temperature to 30 C. and the air fiow and agitation so as to give 3 millimoles of oxygen per litre of culture per minute. The treatment was applied for hours. The cellular density remained 20 grams/litre throughout the experiment. The yeasts were analysed for their fat content at the beginning and end of the process. A marked fall in fat content was observed, from to 5% by wt. on dry matter.
I claim:
1. A process which comprises, in a growth stage, cultivating a straight chain hydrocarbon consuming microorganism in the presence of a hydrocarbon feedstock comprising at least in part straight chain hydrocarbons; in the presence of an aqueous nutrient medium; and in p the presence of a gas containing free oxygen and subsequently recovering a micro-organism free of a substantial amount of hydrocarbon but containing a small amount of hydrocarbon as contaminant, and thereafter in a puri- 'fication stage are carried out in separate fermentation zones.
3. A processing according to claim 1 in which the micro-organism which is cultivated is a yeast.
4. A process according to claim 3 in which the yeast is of the family Cryptococcaceae.
5. A process according to claim 4 in which the yeast is of the subfamily Cryptococcoideae.
6. A process according to claim 5 in which the yeast is of the genus Torulopsis.
7. A process according to claim 4 in which the yeast is of the genus Candida.
8. A process according to claim 5 in which the yeast is Candida lipolytica.
9. A process according to claim 1 in which the microorganism is a "bacteria.
10. A process according to claim 1 in which the feedstock is a petroleum fraction.
11. A process according to claim 1 wherein in the process of recovering the micro-organism free of a substantial amount of hydrocarbon it is necessary to separate the micro-organism from the bulk of unconsurned hydrocarbon.
12. A process according to claim 2 wherein the growth stage and the purification-starvation stage are carried out in separate fermenters.
13. A process according to claim 2 wherein the growth stage and the purification-starvation stage are carried out in different zones of the same fermenter.
References Cited by the Examiner UNITED STATES PATENTS 2,697,061 12/1954 Harris et al. -1 2,697,062 12/1954 Crarner 1951 2,742,398 4/1956 ZoBell 195--3 2,982,692 5/1961 McDill 195-3 3,069,325 12/1962 I-Iitzman 1952 OTHER REFERENCES Cook: The Chemistry and Biology of Yeasts, Academic Press Inc., New York, 1958, pages 648-659.
Lamanna et al.: Basic Bacteriology, The Williams & Wilkins Co., Baltimore, 1953, pages 246256.
Wickerham et al.: Carbon Assimilation Tests for the Classification of Yeasts, Journal of Bacteriology, 56, 1948, pages 363-371.
A. LOUIS MONACELL, Primary Examiner.
D. M. STEPHENS, Assistant Examiner.

Claims (1)

1. A PROCESS WHICH COMPRISES, IN A GROWTH STAGE, CULTIVATING A STRAIGHT CHAIN HYDROCARBON CONSUMING MICROORGANISM IN THE PRESENCE OF A HYDROCARBON FEEDSTOCK COMPRISING AT LEAST IN PART STRAIGHT CHAIN HYDROCARBONS; IN THE PRESENCE OF AN AQUEOUS NUTRIENT MEDIUM; AND IN THE PRESENCE OF A GAS CONTAINING FREE OXYGEN AND SUBSEQUENTLY RECOVERING A MICRO-ORGANISM FREE OF A SUBSTANTIAL AMOUNT OF HYDROCARBON BUT CONTAINING A SMALL AMOUNT OF HYDROCARBON AS CONTAMINANT, AND THEREAFTER IN A PURIFICATION-STARVATION STAGE MAINTAINING SAID MICRO-ORGANISM WITH AN AQUEOUS NUTRIENT MEDIUM AND A GAS CONTAINING FREE OXYGEN IN THE ABSENCE OF AN EXTRANEOUS CARBON SOURCE, WHEREBY THE HYDROCARBON CONTAMINATING THE MICRO-ORGANISM IS REDUCED IN QUANTITY.
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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3427223A (en) * 1964-06-10 1969-02-11 Exxon Research Engineering Co Coagulating microbial cells to enhance their separation
US3489648A (en) * 1966-12-22 1970-01-13 Phillips Petroleum Co Microbial hydrocarbon consumption
US3508927A (en) * 1965-09-15 1970-04-28 Exxon Research Engineering Co Use of unsaturated organic acids as bacterial growth promoters
US3520777A (en) * 1966-05-13 1970-07-14 British Petroleum Co Cultivation and separation of hydrocarbon consuming micro-organisms
US3522147A (en) * 1966-05-13 1970-07-28 British Petroleum Co Growth and separation of hydrocarbon consuming microorganisms
US3620927A (en) * 1969-06-26 1971-11-16 Gulf Research Development Co Cultivation of micro-organisms on hydrocarbons
US3622465A (en) * 1967-03-10 1971-11-23 Allied Chem Protein from normal hydrocarbons
US3642575A (en) * 1966-01-26 1972-02-15 Kyowa Hakko Kogyo Kk Process for producing sugars by fermentation
US3904476A (en) * 1973-05-29 1975-09-09 Mobil Oil Corp Treatment of cells of a hydrocarbon-consuming microorganism

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2697062A (en) * 1951-03-30 1954-12-14 Texaco Development Corp Processing of hydrocarbons
US2697061A (en) * 1950-08-17 1954-12-14 Texaco Development Corp Processing of hydrocarbons
US2742398A (en) * 1951-06-09 1956-04-17 Texaco Development Corp Method of removing deposits of wax and like materials
US2982692A (en) * 1957-06-26 1961-05-02 Hardin B Mcdill Dewaxing of oils
US3069325A (en) * 1959-12-21 1962-12-18 Phillips Petroleum Co Treatment of hydrocarbons

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2697061A (en) * 1950-08-17 1954-12-14 Texaco Development Corp Processing of hydrocarbons
US2697062A (en) * 1951-03-30 1954-12-14 Texaco Development Corp Processing of hydrocarbons
US2742398A (en) * 1951-06-09 1956-04-17 Texaco Development Corp Method of removing deposits of wax and like materials
US2982692A (en) * 1957-06-26 1961-05-02 Hardin B Mcdill Dewaxing of oils
US3069325A (en) * 1959-12-21 1962-12-18 Phillips Petroleum Co Treatment of hydrocarbons

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3427223A (en) * 1964-06-10 1969-02-11 Exxon Research Engineering Co Coagulating microbial cells to enhance their separation
US3508927A (en) * 1965-09-15 1970-04-28 Exxon Research Engineering Co Use of unsaturated organic acids as bacterial growth promoters
US3642575A (en) * 1966-01-26 1972-02-15 Kyowa Hakko Kogyo Kk Process for producing sugars by fermentation
US3520777A (en) * 1966-05-13 1970-07-14 British Petroleum Co Cultivation and separation of hydrocarbon consuming micro-organisms
US3522147A (en) * 1966-05-13 1970-07-28 British Petroleum Co Growth and separation of hydrocarbon consuming microorganisms
US3489648A (en) * 1966-12-22 1970-01-13 Phillips Petroleum Co Microbial hydrocarbon consumption
US3622465A (en) * 1967-03-10 1971-11-23 Allied Chem Protein from normal hydrocarbons
US3620927A (en) * 1969-06-26 1971-11-16 Gulf Research Development Co Cultivation of micro-organisms on hydrocarbons
US3904476A (en) * 1973-05-29 1975-09-09 Mobil Oil Corp Treatment of cells of a hydrocarbon-consuming microorganism

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