Methods for fractionating lipids

Abstract

[Problem] Provision of a method for fractionating lipids using liquefied dimethyl ether as a solvent. [Means for Solving] To provide a method for fractionating a lipid using liquefied dimethyl ether as a solvent. [Solution] A method for fractionating a lipid, which comprises subjecting a microbial biomass to extraction using liquefied dimethyl ether as a solvent and then fractionating the lipid utilizing separation selectivity for the lipid. A method for producing a lipid, which comprises subjecting a microbial biomass to extraction using liquefied dimethyl ether as a solvent, then fractionating a portion of the lipid utilizing separation selectivity for the lipid to modify the fatty acid composition of the remainder of the lipid which remains in the microbial biomass, and then extracting the lipid having a modified fatty acid composition.

Claims

1. A method for fractionating lipids during extraction of the lipids from a microbial biomass, comprising extracting lipids from the microbial biomass using liquefied dimethyl ether as a solvent; collecting two or more fractions of extracts, wherein the two or more fractions have a fatty acid composition which is different from each other, and wherein the two or more fractions have a different proportion of contents of saturated fatty acids and highly unsaturated fatty acids from each other; and removing the liquefied dimethyl ether from each of the two or more fractions.

2. The method according to claim 1, wherein the microbial biomass is biomass obtained by culturing a microorganism in the class Labyrinthulea.

3. The method according to claim 2 wherein the microorganism in the class Labyrinthulea belongs to the genus Aurantiochytrium.

4. The method according to claim 1, wherein the microbial biomass is biomass obtained by culturing a microorganism in the class of green algae.

5. The method according to claim 4 wherein the microorganism in the class of green algae belongs to the genus Haematococcus.

6. The method according to claim 4, wherein the two or more fractions have a different proportion of contents of chlorophyll and astaxanthin from each other.

7. The method according to claim 1, wherein the extraction from microbial biomass with the liquefied dimethyl ether is performed by using a column.

8. The method according to claim 1, wherein the extraction from microbial biomass with the liquefied dimethyl ether is performed by a batch process.

9. A method for altering composition of lipids in microbial biomass comprising, extracting the microbial biomass with liquefied dimethyl ether as a solvent; and selectively decreasing the proportion of first lipids in the microbial biomass and concentrating second lipids in the microbial biomass, by making use of the separation selectivity of the liquefied dimethyl ether for lipids of microbial biomass and altering the fatty acid composition in the microbial biomass, wherein the first lipids are saturated fatty acids and the second lipids are highly unsaturated fatty acids.

10. A method for producing lipids comprising, extracting the second lipids from the microbial biomass having the altered composition of lipids by the method of claim 9.

11. The method according to claim 10, wherein the microbial biomass is biomass obtained by culturing a microorganism in the class Labyrinthulea.

12. The method according to claim 11 wherein the microorganism in the class Labyrinthulea belongs to the genus Aurantiochytrium.

13. The method according to claim 10, wherein the microbial biomass is biomass obtained by culturing a microorganism in the class of green algae.

14. The method according to claim 13 wherein the microorganism in the class of green algae belongs to the genus Haematococcus.

15. The method according to claim 9, wherein the microbial biomass is biomass obtained by culturing a microorganism in the class Labyrinthulea.

16. The method according to claim 15 wherein the microorganism in the class Labyrinthulea belongs to the genus Aurantiochytrium.

17. The method according to claim 9, wherein the microbial biomass is biomass obtained by culturing a microorganism in the class of green algae.

18. The method according to claim 17 wherein the microorganism in the class of green algae belongs to the genus Haematococcus.

Description

BRIEF DESCRIPTION OF DRAWINGS

(1) FIG. 1 is a schematic diagram showing one mode of an apparatus to be used in the present invention.

DESCRIPTION OF EMBODIMENTS

(2) In the present invention, intracellular lipids of microbial biomass are recovered through fractionation by making use of the differential selectivity of liquefied DME for lipids.

(3) The liquefied DME (IUPAC name: methoxymethane) to be used in the present invention has a boiling point of 23.6 C., so it assumes the gaseous state at normal temperature. The gas is brought back to the liquid state for use as a solvent in the present invention. To liquefy DME, adjustments can be appropriately made within the ranges of from about 0.25 to about 1.14 MPa for pressure and from about 0 to about 50 C. for temperature.

(4) The term microorganism as used in the present invention refers to those microorganisms which produce lipids in their cells. Examples are microorganisms that belong to the genera Crypthecodinium, Thraustochytrium, Schizochytrium, Ulkenia Japonochytrium, Haliphthoros, Mortierella, Penicillium, Aspergillus, Rhodotorula, and Fusarium. Specific examples are microorganisms such as the dinoflagellate Crypthecodinium cohnii, the labyrinthelea Aurantiochytrium limacinum (also known as Schizochytrium limacinum) and the filamentous fungus Mortierella alpina, as well as the green alga Haematococcus pluvialis.

(5) The term lipids as used in the present invention refers to those lipids which are produced by microorganisms and typical examples include triglycerides, diglycerides, monoglycerides, phospholipids, free fatty acids, sterols, hydrocarbons, etc. If desired, components like pigments contained in microorganism-produced lipids, such as astaxanthin and other carotenoids, can also be fractionated together with the lipids.

(6) The composition of fatty acids bound to lipids varies with the microorganism but, typically, fatty acids having 12-24 carbon atoms and 0-6 double bonds are contained in varying proportions. Fatty acids that have physiological activities and are held useful are highly unsaturated fatty acids, which are fatty acids having at least 18 carbon atoms and at least 3 double bonds, more preferably fatty acids having at least 20 carbon atoms and at least 3 double bonds. Specific examples include -linolenic acid (18:3, n-3), -linolenic acid (18:3, n-6), arachidonic acid (20:4, n-6), di-homo--linolenic acid (20:3, n-6), eicosapentaenoic acid (20:5, n-3), docosapentaenoic acid (22:5, n-6), docosahexaenoic acid (22:6, n-3), etc.

(7) Lipids in microbial cells have these fatty acids bound thereto as constituent fatty acids in triglycerides, phospholipids, or the like.

(8) The simplest way to make use of the separation selectivity of liquefied DME for lipids comprises packing a column with microbial cells, causing liquefied DME to flow through the column at a specified rate, and fractionating the effluent. As will be shown in Examples later, liquefied DME offers selectivity in the process of eluting lipids from the microbial cells.

(9) Liquefied DME allows for early elution of lipids that contain saturated fatty acids whereas the elution of lipids that contain highly unsaturated fatty acids is delayed. This difference in elution rate is effectively used to increase the concentration of highly unsaturated fatty acids contained in the lipids. The same result can be obtained without using the column but by a batch process repeating runs of extraction with a small amount of liquefied DME. Any other type of apparatus may be employed if it exhibits the same effect.

(10) In the conventional case of solvent extraction from microbial cells, high efficiency is realized in extraction by using hexane, for example, but since hexane has only low separation selectivity for lipids, the composition of fatty acids in the extracted neutral lipids is basically the same as the composition of fatty acids in the neutral lipids in the microbial biomass. If the highly unsaturated fatty acids in the extracted lipids need to be concentrated, a separate purification step is performed after the extraction. Known methods of purification that can alter the composition of fatty acids include urea adduct separation methods, winterization, precision distillation, and lipase-based concentration, and these methods share the principle of altering the composition of fatty acids on the basis of differences in their properties such as molecular weight or the number of unsaturated bonds.

(11) According to the method of the present invention, highly unsaturated fatty acids can already be concentrated to a certain extent at the stage of extraction from the microbial biomass. If desired, separation by the method of the present invention may be followed by purification by the above-described conventional methods.

(12) The above-described separation selectivity of liquefied DME can be utilized to selectively remove saturated and other unwanted fatty acids by extraction from microbial cells and, thereafter, all of the remaining lipids are extracted with hexane or other organic solvents.

(13) By means of fractionation with liquefied DME, pigments such as astaxanthin that are contained in lipids are concentrated together with the lipids that are rich in those pigments and may be immediately used as concentrated pigments; alternatively, they may be further purified by applying methods for astaxanthin purification such as extraction with supercritical carbon dioxide.

(14) On the following pages, working examples of the present invention will be described but it should be understood that the present invention is by no means limited to these examples.

(15) The structural setup of the extraction apparatus used in the working examples is shown in FIG. 1. An extraction column to be packed with a microorganism (HPG-10-5; product of TAIATSU TECHNO; 180 mm26 mm (i.d.)) was connected at the outlet to a storage vessel (HPG-96-3; product of TAIATSU TECHNO; capacity 96 cm.sup.3) by means of a stainless steel tube. The extraction column and the storage vessel were each a pressure-resistant vessel made of glass and a polycarbonate resin. Liquefied dimethyl ether as supplied from a dimethyl ether tank was flowed to the extraction column packed with microbial cells and the extract from the extraction column was recovered into the storage vessel. After extraction was performed for a prescribed time, the pressure reducing valve on the storage vessel was opened, whereupon dimethyl ether was evaporated away to leave a mixture of the extract and water, which was then recovered from the storage vessel.

Example 1

Extraction of Lipids from Labyrinthulea

(16) An inoculum of Aurantiochytrium limacinum, a microorganism belonging to the class Labyrinthulea, was cultured in a GY medium (30 g glucose and 10 g yeast extract were dissolved in 1 L of 50% artificial seawater and adjusted to pH 7.0). Specifically, 30 mL of the GY medium was poured into a 50 mL Erlenmeyer flask and cultured for 3 days at 28 C. with shaking at 100 rpm. Cells were collected from the culture broth by centrifugation, washed with distilled water to remove the medium components, and cells were collected by further centrifugation. The collected cells were lyophilized to make microbial biomass. The thus obtained microbial biomass was stored in a freezer at 20 C. until it was subjected to extraction.

(17) To 0.33 g of the lyophilized microbial biomass, 1.263 g of distilled water was added and the mixture was stirred well to make a sample, which was subjected to extraction, with fractionation being performed, using the apparatus of FIG. 1. In the process, the flow rate of liquefied dimethyl ether was set at 5 mL/min. The temperature of the extraction column was set at 20 C. and the pressure at 0.51 MPa. The microbial biomass was rendered hydrous through addition of distilled water and this was in order to reproduce the state of microbial cells that were close to those which had been collected from the culture broth. In the process, no operation was conducted for disrupting cells.

(18) The extract was fractionated at the time intervals indicated in Table 1. The respective fractions obtained by flowing liquefied dimethyl ether were reverted to normal temperature and pressure, whereupon the dimethyl ether was evaporated away from the extract in each fraction. Subsequently, a dried gas (which was dimethyl ether in Example 1) was brought into adequate contact with the extract, so that moisture was removed from the extract in each fraction to give oils in the amounts indicated in Table 1.

(19) TABLE-US-00001 TABLE 1 Fraction No. 1 2 3 4 5 6 Total Time (min) 2 7 17 33 49 65 Oil (mg) 12 32 33 10 9 1 97 Note: The weights of oils with fraction Nos. 1 to 6 are found values and the total weight is a calculated value.

(20) From the thus obtained oils, fatty acid methyl esters were prepared and subjected to gas chromatographic analysis of the composition of fatty acids. For the analysis, a gas chromatograph (Agilent Technologies 7890A GC System) and a column (J&W DB-WAX; 0.25 mm i.d. 30 m long, with film thickness of 0.25 m) were used under such conditions that the column temperature (gradient) was 140 C..fwdarw.240 C. (4 C./min), with holding at 240 C. for 10 minutes, and that He was used as a carrier gas (1.05 ml/min). The results of the analysis are shown in Table 2. The composition of fatty acids turned out to vary greatly between oils, clearly showing that the method of extraction using liquefied dimethyl ether as a solvent had separation selectivity for lipids.

(21) The oils of fraction Nos. 1 and 2 in Table 2 had extremely high values (ca. 80%) for palmitic acid (C16:0) in the composition of fatty acids. The values were higher than that for palmitic acid in the composition of fatty acids as calculated from the sum of the oils in all fractions of Example 1. Therefore, it became clear that the method of extraction using liquefied dimethyl ether as a solvent is capable of fractionation for increasing the proportion of palmitic acid containing lipids which are expected as a biofuel.

(22) What is more, the oils of fraction Nos. 3, 4 and 5 in Table 2 showed higher values for DHA in the composition of fatty acids than that for DHA in the composition of fatty acids as calculated from the sum of the oils in all fractions of Example 1. Therefore, it became clear that the method of extraction using liquefied dimethyl ether as a solvent is capable of fractionation for increasing the proportion of DHA containing lipids.

(23) TABLE-US-00002 TABLE 2 Composition Fraction No. of fatty acids (%) 1 2 3 4 5 6 Total C14:0 7.0 6.8 3.8 3.9 3.8 3.6 5.2 C16:0 78.0 78.8 45.1 46.6 41.4 43.7 60.1 C18:0 2.9 2.8 1.6 1.9 2.8 4.2 2.3 DPA n-6 1.4 1.5 8.9 7.8 7.1 4.8 5.2 DHA 4.7 4.1 33.8 29.2 25.4 16.3 19.0 Others 6.0 6.0 6.8 10.7 19.5 27.5 8.2 Note: The compositions of fatty acids in the oils with fraction Nos. 1 to 6 are found values and the total compositions of fatty acids are calculated values.

Example 2

Method for Obtaining DHA Concentrated Microbial Oil by Selective Extraction Using Dimethyl Ether

(24) The results of Example 1 suggested the possibility for selectively removing C16:0 and like fatty acids from microbial biomass by extraction while allowing the other fatty acids like DHA to remain in the biomass.

(25) The microbial biomass used in Example 1 contained the oil identified in the column of Feed in Table 3. When this biomass is subjected to only the extraction of up to fraction No. 2 in Table 2, the resulting biomass will contain, by calculation, a residual oil of the composition indentified in the column of Biomass after extraction in Table 3.

(26) From Table 3, it can be seen that by extracting lipids with an increased proportion of palmitic acid containing lipids by the method of extraction using liquefied dimethyl ether as a solvent, it is possible to increase the proportion in the microbial biomass of lipids containing other fatty acids, say, DHA.

(27) The microbial biomass may be used as a feed for further extraction and subjected to extraction with a solvent such as hexane that has low separation selectivity for lipids, whereby lipids with an increased proportion of DHA containing lipids can be extracted with good efficiency.

(28) TABLE-US-00003 TABLE 3 Biomass after Feed extraction Oil (mg) 149 105 Composition of fatty acids (%) C14:0 3.9 2.6 C16:0 47.8 34.3 C18:0 1.6 1.0 DPA n-6 8.8 12.0 DHA 33.9 46.8 Others 4.2 3.3

Example 3

Extraction of Lipids from Haematococcus Alga

(29) Dried biomass of Haematococcus alga purchased from Biogenic Co., Ltd. (Haematococcus pluvialis, BM070828, yet to be disrupted) was used as microbial biomass and subjected to extraction. To 0.403 g of the microbial biomass, 2.317 g of distilled water was added and the mixture was well stirred to make a sample, which was subjected to extraction using the apparatus of FIG. 1. In the process, the flow rate of liquefied dimethyl ether was set at 10 mL/min. The temperature of the extraction column was set at 20 C. and the pressure at 0.51 MPa. In the process, no operation was conducted for disrupting cells. The amounts of the oils obtained by the same procedures as in Example 1 are shown in Table 4, and the results of subjecting those oils to analysis of the composition of fatty acids are shown in Table 5. The composition of fatty acids turned out to vary greatly between oils, clearly showing that as in Example 1, the method of extraction using liquefied dimethyl ether as a solvent had separation selectivity for lipids.

(30) From the results of Examples 1 and 3, it became clear that the method of fractionating lipids by utilizing the separation selectivity for lipids of liquefied dimethyl ether used as the solvent can be operated independently of the type of microorganisms.

(31) TABLE-US-00004 TABLE 4 Fraction No. 1 2 3 4 5 6 Total Time (min) 3.3 6.3 10.2 14.6 20.9 26.3 Oil (mg) 18.2 2.6 4.4 1.8 2.4 1.6 31.0

(32) TABLE-US-00005 TABLE 5 Composition Fraction No. of fatty acids (%) 1 2 3 4 5 6 C14:0 0.7 1.2 0.6 0.7 0.9 0.8 C16:0 39.4 22.0 18.0 9.2 10.9 8.5 C18:0 2.7 6.1 4.9 4.7 6.7 4.0 C18:1 n-9 15.2 10.8 9.4 4.0 4.3 3.5 C18:2 n-6 9.5 9.0 8.7 3.0 2.9 2.5 C18:3 n-6 1.2 4.6 4.2 3.9 5.5 7.9 C18:3 n-3 2.6 2.8 2.9 1.0 1.1 0.9 Others 28.8 43.5 51.3 73.5 67.7 71.9

(33) The weight of astaxanthin in each of the oils obtained in Example 3 was measured by HPLC. An astaxanthin standard compound and the respective oils were dissolved in acetone:chloroform=2:1 for analysis. The conditions for analysis were as follows: column, COSMOSIL 2504.6 mm (i.d.), 5C.sub.18-MS-PAQ type (product of Nacalai Tesque, Inc.); detector, Intelligent UV/visible light detector UV-2075 plus (product of JASCO Corporation); mobile phase, methanol:tetrahydrofuran=9:1; flow rate, 1.5 mL/min; detection, 470 nm). The results are shown in Table 6. The colors of the respective oils as seen by visual inspection are also indicated in Table 6. Haematococcus pluvialis is a microalga belonging to the class of green algae and contains the lipid soluble pigment chlorophyll (green) as a photosynthetic pigment. It is also known that astaxanthin (red orange) which is another lipid soluble pigment accumulates at high concentration in cyst cells of Haematococcus pluvialis. Since the respective oils obtained by extraction using liquefied dimethyl ether as the solvent had distinct color differences, the liquefied dimethyl ether was even verified to have separation selectivity for those lipid soluble pigments. This property of liquefied dimethyl ether may be used to provide a method by which the content of chlorophyll, for example, is reduced, eventually producing an astaxanthin containing oil that presents a brighter, red orange color.

(34) TABLE-US-00006 TABLE 6 Fraction No. 1 2 3 4 5 6 Astaxanthin 11.2 10.0 3.2 1.3 0.9 1.1 (g) Color (to the eye) green orange orange blackish orange light orange to green orange

INDUSTRIAL APPLICABILITY

(35) In accordance with the present invention, it is possible to extract lipids from microbial biomass containing useful, highly unsaturated fatty acids and at the same time fractionate lipids that are rich in saturated fatty acids and the lipids that are rich in highly unsaturated fatty acids. The present invention provides a method that uses liquefied dimethyl ether not as a mere extraction solvent but as a solvent that performs both extraction and fractionation.