JP5617141B2 - Method for producing phospholipid - Google Patents

Description

The present invention relates to a method for producing a phospholipid, the production method of the phosphorus lipid relates particularly edible.

  Recent research on lipids revealed that highly unsaturated fatty acids such as docosahexaenoic acid (DHA) and eicosapentaenoic acid (EPA) have various functions such as improved learning function, prevention of arteriosclerosis, and lipid metabolism improvement function. ing. In particular, when DHA is ingested in a form bound to a phospholipid such as phosphatidylcholine, it has a strong anti-oxidation property and stability as compared with the triglyceride type, and because it absorbs well, the physiological activity of DHA is easily expressed. It has become clear. EPA other than DHA and functional fatty acids such as conjugated linoleic acid and arachidonic acid can also be expected to increase physiological activity by binding to phospholipids.

  The method for producing phospholipids to which functional fatty acids such as DHA are bound is divided into a method for extracting naturally occurring ones and a method for synthesizing soybean phospholipids as raw materials. Specifically, there are a method of extracting DHA-binding phospholipids from aquatic animal eggs as a raw material (Patent Document 1), a method of extracting from marine products such as squid with an organic solvent, and the like (Patent Document 2).

  However, in these methods, the raw materials are expensive, the supply is not always stable, and the composition of phospholipids depends on the raw materials, so that it is possible to produce a product in which a functional fatty acid other than DHA is bound. Can not.

  As a method for introducing a desired fatty acid regardless of the composition of the raw material, there is a method of adding a desired fatty acid to a microorganism culture solution and producing a phospholipid in which the fatty acid is incorporated (Patent Document 3). In this method, only a small amount of phospholipid can be obtained from a large amount of culture solution, and the production efficiency is not good.

  On the other hand, as a method of binding DHA to soybean phospholipid or the like, there is a method of adding a high dielectric constant hydrogen bond-forming product to a reaction system of lipase and phospholipase (Patent Document 4). In this method, lysophospholipid by lipase is used. Although a high reaction rate was obtained by the reaction of fatty acid and fatty acid, a high reaction rate was not obtained by the reaction with phospholipase A2. It is important that DHA binds to the 2-position of phospholipid for the expression of the physiological activity of DHA-bound phospholipid. Since the target fatty acid binds mainly to the 1-position of phospholipid in the lipase reaction, It cannot be said that it is highly practical.

  In addition, as a method for introducing a fatty acid into the 2-position of phospholipid with a high reaction rate using phospholipase A2, a method of reacting with toluene as a solvent (Non-patent Document 1), a method of reacting in a system in which glycerin and formamide are added (non- Patent Document 2) can be mentioned, but these are not suitable for food applications because of the use of harmful substances such as toluene and formamide.

  Therefore, using only raw materials that can be used for food, a method capable of introducing a fatty acid into the 2-position of the phospholipid with a high reaction rate, in particular, a phospholipid in which a highly unsaturated fatty acid such as DHA is introduced into the 2-position, and a process for producing the same. Is desired.

JP-A-8-59678 JP-A-8-325192 JP 2007-129773 A JP-A-8-56683

Biochimica et, Biophysica Acta 1997, 1343, 76-84. Fishers Science 2006, 72, 909-911.

An object of the present invention provides a method for producing Li phospholipids efficiently bound with any fatty acid, particularly 2-position of efficiently phospholipids using safe raw material suitable for food applications among various applications That is.

  As a result of intensive studies to solve the above-mentioned problems, the present inventors have efficiently reacted by adding an amino acid to the reaction system in the reaction of lysophospholipid and fatty acid in a system containing phospholipase A2. It was found that a large amount of phospholipid obtained by introducing a desired fatty acid into position 2 of lysophospholipid can be obtained, and the present invention has been completed.

  That is, in the first aspect of the present invention, in the esterification reaction of lysophospholipid with phospholipase A2, the esterification reaction is performed in glycerin, and an amino acid and / or a peptide having 3 or less amino acids is added to the reaction system. The present invention relates to a method for producing phospholipids. The method for producing phospholipid as described above, wherein the amino acid is at least one selected from the group consisting of glycine, alanine, asparagine, glutamine, isoleucine, leucine, serine, threonine, valine, phenylalanine, and tyrosine; The method for producing a phospholipid according to the above, wherein the peptide below the residue is a peptide comprising a combination of glycine, alanine, and serine, the method for producing the phospholipid according to the above, wherein the esterification reaction is performed at 35 ° C. or more and 80 ° C. or less, The said lysophospholipid is related with the manufacturing method of the said phospholipid as described in a soybean.

  Further, after the esterification reaction, a ketone solvent is added to form a glycerin solution layer and a ketone solvent layer, the ketone solvent layer is separated, and then the solvent in the ketone solvent layer is distilled off, and then the fatty acid is removed. The method for producing a phospholipid as described above for obtaining phospholipid, after adding an alcohol having 4 or less carbon atoms after the esterification reaction, adding a solvent comprising a hydrocarbon solvent and / or a ketone solvent and / or an ester solvent to add glycerin A solution layer and a solvent layer are formed, the solvent layer is separated, and then the solvent in the solvent layer is distilled off, and the fatty acid is removed to obtain a phospholipid. The present invention relates to a method for producing a phospholipid as described above, which is acetone, and a method for producing a phospholipid as described above, wherein the alcohol having 4 or less carbon atoms is ethanol.

  In the third aspect of the present invention, an amino acid and / or a peptide having 3 or less amino acids is mixed with a reaction system containing lysophospholipid obtained by hydrolyzing the 2-position of phospholipid with phospholipase A2. Thus, the present invention relates to a method for introducing a fatty acid into the 2-position of a phospholipid by conducting an esterification reaction of lysophospholipid with phospholipase A2.

According to the present invention, it is possible to provide a method for efficiently producing efficiently phosphorus lipid bound with any fatty acid in the 2-position of phospholipids using a safe raw material.

  Hereinafter, the present invention will be described in more detail. The phospholipid of the present invention can be produced by adding an amino acid and / or a peptide having 3 or less amino acids to the reaction system in the esterification reaction of lysophospholipid with phospholipase A2.

  The lysophospholipid in the present invention refers to a phospholipid obtained by removing the fatty acid at the 2-position, and means a lipid different from the phospholipid. As the lysophospholipid used in the present invention, a phospholipid-modified one can be used. From the viewpoint of availability, those derived from soybean, rapeseed, and egg yolk are preferable, and those derived from soybean from the price aspect. More preferably, other plant-derived lysophospholipids can also be used.

  The method of modifying the phospholipid to remove the fatty acid at the 2-position is not particularly limited as long as no harmful substance is used. For example, a method of hydrolyzing the fatty acid at the 2-position of phospholipid using phospholipase A2 or the like Etc. The phospholipid that can be used in this case is a molecule having a glycerin skeleton, a phosphate group, and two fatty acid esters, which can be a substrate for phospholipase A2, and does not include those having a sphingosine skeleton. Specific examples include phosphatidylcholine, phosphatidylethanolamine, phosphatidylserine, and the like.

  In the esterification reaction of lysophospholipid and fatty acid performed in the present invention, the fatty acid to be introduced at the 2-position of lysophospholipid is not particularly limited, but from the recent consumer health orientation, fatty acids that can enhance physiological activity are preferable, Highly unsaturated fatty acids such as conjugated linoleic acid, arachidonic acid, docosahexaenoic acid (DHA), and eicosapentaenoic acid (EPA) can be exemplified. As the DHA and EPA, those obtained by hydrolyzing fats and oils obtained mainly from marine animal oils and algae to form free fatty acids can be used.

  In the present invention, the highly unsaturated fatty acid means an unsaturated fatty acid having 3 or more carbon-carbon double bonds or conjugated linoleic acid.

  The fatty acid used in the present invention is preferably 30 to 1000 parts by weight with respect to 100 parts by weight of phospholipid. If the amount is less than 30 parts by weight, a large amount of lysophospholipid not bound with fatty acid may remain after the reaction and the reaction efficiency may deteriorate, and if it exceeds 1000 parts by weight, it may be disadvantageous in terms of cost.

  In addition, when it is difficult to obtain a naturally derived material alone such as DHA, a mixture of fatty acids containing a desired fatty acid can be used. At that time, the content of the desired fatty acid in the fatty acid mixture is desirably approximately 20% by weight or more. In the case of DHA, the concentration of DHA in the DHA-containing fatty acid is preferably 20% by weight or more, and more preferably having a DHA concentration of 45% by weight or more. The concentration of the phospholipid as a reaction product may be increased by performing solvent fractionation after the esterification reaction according to the present invention.

  The phospholipase A2 used in the present invention is not particularly limited in its origin, but those that can be generally used for food are preferable, and examples thereof include those derived from porcine pancreas and microorganisms.

  The amino acid used in the present invention refers to a molecule that mainly serves as a component of a protein and has a carboxyl group and an amino group in the molecule, and is preferably an edible one. Among them, neutral amino acids are preferable because the enzyme can be activated without relatively affecting the charge state of the enzyme, and examples include glycine, alanine, asparagine, glutamine, isoleucine, leucine, serine, threonine, valine, phenylalanine, and tyrosine. In addition, when used in the method for producing a phospholipid of the present invention, at least one selected from these groups can be used.

  A peptide having 3 or less amino acids used in the present invention refers to a peptide in which amino acids are mainly dimerized or trimerized by an amide bond and is synthesized from amino acids, or a protein is converted to an enzyme, etc. However, it is preferably a peptide composed of glycine, alanine, and serine because of its relatively high solubility in glycerin, and examples thereof include glycylglycine.

  In the present invention, as described above, one of the features is that the amino acid is a peptide having 3 or less residues. The reason for this is that the smaller the amino acid residue, the higher the molar concentration when dissolved in glycerin. This is because the resulting phospholipase A2 can be efficiently activated.

  It is sufficient that at least one of the amino acids and peptides having 3 or less amino acids as described above is added in the esterification reaction of lysophospholipid with phospholipase A2, and the amount added is 100 parts by weight of lysophospholipid. It is preferable to add 10 to 2000 parts by weight, more preferably 50 to 500 parts by weight. If it is less than 10 parts by weight, the reaction efficiency may be deteriorated, and if it exceeds 2000 parts by weight, the cost may be disadvantageous and the reaction efficiency may be deteriorated. Furthermore, amino acids or peptides having 3 or less amino acids may be added in combination of two or more in order to increase the total amount of dissolution in the esterification reaction system.

  In the present invention, an antioxidant may be added as necessary. Antioxidants that can be used in the present invention can be used for food, and any type can be used as long as they can be expected to have an antioxidant power against fatty acids such as DHA, but polyphenols such as tocopherol and catechin, ascorbic acid, and dibutyl Hydroxytoluene (BHT) or the like is preferably used. In this case, the phospholipid obtained by the production method described later may be a mixture with an antioxidant.

  Similarly, in order to prevent fatty acid oxidation, the esterification reaction of lysophospholipid may be performed in a nitrogen atmosphere while blocking oxygen.

  In this invention, although the said esterification reaction can be performed using the solvent which can melt | dissolve an amino acid, it can be used for a foodstuff and uses highly polar glycerol.

One preferred example of the method for producing a phospholipid of the present invention is shown below.
First, a fatty acid such as lysophospholipid and DHA is dissolved in glycerin, and an esterification reaction of lysophospholipid is performed by adding an amino acid or / and a peptide having 3 or less amino acids and phospholipase A2 and stirring. At this time, calcium ions are preferably present in the reaction system for the activation of the enzyme. As the calcium source, calcium chloride is preferable because it has a relatively high solubility and is used as a food material.

  At this time, the esterification reaction of lysophospholipid by phospholipase A2 is preferably performed in a temperature range of 35 ° C. to 80 ° C. from the viewpoint of optimal enzyme temperature and fatty acid oxidation, and in the range of 45 ° C. to 70 ° C. More preferably. In addition, in order to prevent fatty acid oxidation during the reaction, an antioxidant may be added in advance to perform esterification of lysophospholipid, or the reaction may be performed in a nitrogen atmosphere with oxygen blocked. These may be used alone or in combination. Further, in the reaction with phospholipase A2, when hydrolysis proceeds excessively, for example, when the reaction proceeds, water may be removed by appropriately performing an operation such as decompression during the reaction. When moisture is removed by decompression, the conditions may be, for example, a temperature of 35 to 80 ° C. and 150 torr (20 kPa) or less for 12 to 24 hours. The progress of the esterification reaction can be confirmed by thin layer chromatography (TLC) or the like.

  By performing esterification reaction of lysophospholipid and fatty acid as described above, the phospholipid of the present invention in which a desired fatty acid is introduced at the 2-position of lysophospholipid is produced. In the present invention, even in the state of the reaction solution as described above, it can be used as a phospholipid solution for various uses. However, a highly purified phospholipid can also be obtained by performing an extraction operation described later.

In the present invention, the following operation is preferably performed as an extraction operation for obtaining a highly pure phospholipid.
That is, a solvent composed of a hydrocarbon solvent and / or a ketone solvent and / or an ester solvent is added to the reaction solution after the completion of the esterification reaction to form a glycerin solution layer and a solvent layer. At this time, phospholipids and fatty acids are transferred to the solvent layer (upper layer), and other substances are transferred to the glycerol solution layer (lower layer). Then, the solvent layer is separated (sorted). Note that the addition of the predetermined solvent and the preparative operation may be repeated as appropriate in consideration of improvement in purity and work efficiency.

  Here, the hydrocarbon solvent refers to a compound that can be used as a solvent among compounds composed only of carbon and hydrogen. Specifically, pentane, hexane, heptane and the like are preferable, but hexane is more preferable because it has a low boiling point and can be easily distilled off and used as a food additive.

  The ketone solvent refers to a molecule that has a keto group in the molecule and can be used as a solvent. Specific examples include acetone and butanone, but acetone is preferable because it has a low boiling point and can be easily distilled off and used as a food additive.

  Further, the ester solvent refers to those having an ester bond in the molecule and usable as a solvent, specifically, methyl acetate, ethyl acetate, etc., but ethyl acetate is preferable because it is used for food use. .

  In the present invention, it is preferable to add an alcohol having 4 or less carbon atoms after the above esterification reaction and before adding the solvent. This tends to prevent hydrolysis during the extraction operation, deactivate phospholipase A2, and lower the viscosity of glycerin to facilitate extraction. In addition, when using the solvent which consists only of the said ketone solvent as said solvent, since the influence of the hydrolysis in the above extraction operation, the activity of phospholipase A2, and the viscosity of glycerol is low, it does not add the said alcohol. May be.

  Here, the alcohol having 4 or less carbon atoms refers to methanol, ethanol, propanol and butanol, and ethanol is preferable because it has low toxicity and can be used as a food additive.

  The method for removing the fatty acid after separating (sorting) the solvent layer as described above is not particularly limited, and a method of degreasing with a ketone solvent, an ethanol-hexane mixed solvent, or the like, a method of removing the fatty acid using silica gel Etc. can be exemplified.

  For example, as a method using a ketone solvent, etc., after the solvent in the separated (prepared) solvent layer is distilled off, a new ketone solvent is added separately and cooled to precipitate phospholipids and dissolve fatty acids. By separating and removing the obtained ketone solvent, it is possible to obtain the phospholipid of the present invention having high purity in which a desired fatty acid is introduced at the 2-position of the lysophospholipid. Here, the ketone solvent added after the solvent is distilled off is preferably acetone which has a low boiling point, can be easily distilled off and can be used as a food additive.

  In addition, as a method of removing fatty acid using silica gel, after separating the solvent layer, the solvent layer is passed through a column filled with silica gel to adsorb phospholipids, and the fatty acid is allowed to flow out. The phospholipid adsorbed on the silica gel was desorbed by flowing the effluent solvent, and only the desired phospholipid fraction was collected, and then the phospholipid was recrystallized to introduce the desired fatty acid at the 2-position of the lysophospholipid. Thus, the highly purified phospholipid of the present invention can be obtained.

  The present invention includes a case where phospholipid is used as a starting material instead of directly using lysophospholipid. For example, after hydrolyzing position 2 of phospholipid with phospholipase A2, the obtained lysophospholipid, an amino acid and / or a peptide having 3 or less amino acids, and a desired fatty acid are reacted in glycerin, and lysoline by phospholipase A2 By performing the esterification reaction of the lipid, the fatty acid at the 2-position of the phospholipid can be exchanged for the desired fatty acid.

  The method for producing phospholipids of the present invention can be suitably used for the production of edible phospholipids. For this purpose, it is only necessary to use raw materials that are not edible or solvents such as toluene and formamide in the production process. . In addition, the phospholipid thus obtained, in particular, a product in which a highly unsaturated fatty acid is introduced at the 2-position thereof can be suitably used as a high-functional edible phospholipid.

  EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to these examples.

<Measurement of fatty acid composition of phospholipid>
In Examples and Comparative Examples, after completion of the esterification reaction, 50 μl of the reaction solution was added with 50 μl of ethanol and 0.5 ml of saturated sodium chloride solution and stirred, and phospholipid, lysophospholipid and fatty acid were extracted with 200 μl of hexane four times. Repeated. An organic layer containing phospholipids, lysophospholipids and fatty acids is developed by TLC (thin layer chromatography), phospholipids and lysophospholipid fractions are separated, methyl esterified with sodium methylate, and phospholipids and lysolin The fatty acid composition of the fatty acid bound to the lipid was measured by gas chromatography (“GC-14B” manufactured by Shimadzu Corporation), and the area ratio corresponding to each fatty acid was defined as the weight ratio of the fatty acid composition in the entire fatty acid composition.

<Measurement of extraction ratio of phospholipid and lysophospholipid>
Each upper layer and chloroform-methanol layer (lower layer separated from acetone layer) obtained in Examples 9 to 13 and Comparative Examples 7 to 8 were dissolved in 50 μl of a solvent of chloroform: methanol = 2: 1, and 2 μl each was added to TLC. The spots of phosphatidylcholine and lysophosphatidylcholine were calculated using image analysis software “ImageJ”, and the extraction ratio for each phosphatidylcholine and lysophosphatidylcholine was expressed as a percentage so that the total of each layer was 100%.

<Comprehensive evaluation of each extraction method>
In Examples 9 to 13 and Comparative Examples 7 to 8, the phosphatidylcholine extract ratio (x) in each upper layer obtained by the extraction ratio measurement of the phospholipid / lysophospholipid is better as it is larger. The smaller the lysophosphatidylcholine extraction ratio (y), the better and the evaluation was based on the following criteria. Evaluation point is
Regarding x, 5 points: 100%>x> 80%, 4 points: 80% ≧ x> 60%, 3 points: 60% ≧ x> 40%, 2 points: 40% ≧ x> 20%, 1 point : 20% ≧ x,
Regarding y, 3 points: 30% ≧ y, 2 points: 60% ≧ y> 30%, 1 point: y> 60%
And the overall evaluation as the extraction method as the sum of the evaluation points,
A: (evaluation point of x) + (evaluation point of y) ≧ 7, that is, a sufficient amount of reacted phospholipid is extracted, and the extraction amount of unreacted lysophospholipid is small and a high quality phospholipid is obtained. Was
○: 7 points> (x evaluation point) + (y evaluation point) ≧ 6 points, that is, a sufficient amount of reacted phospholipids was extracted,
Δ: 6 points> (x evaluation point) + (y evaluation point) ≧ 5 points, that is, the extracted amount of the reacted phospholipid is insufficient.
X: 5 points> (evaluation point of x) + (evaluation point of y), that is, the extracted amount of the reacted phospholipid is remarkably insufficient.
It was.

Example 1
97 mg of oleic acid (manufactured by Tokyo Chemical Industry Co., Ltd.) and 1 g of glycerin (manufactured by Sakamoto Pharmaceutical Co., Ltd.) are added to 35 mg of lysophosphatidylcholine (“SLP-LPC70H” manufactured by Sakai Oil Co., Ltd.), and 50 mg of glycine (manufactured by Wako Pure Chemical Industries, Ltd.) is further added. Was added. Furthermore, 10 mg of phospholipase A2 (“Lecitase 100S” manufactured by Novozymes Japan, 130 Iu / mg) and 2.5 μl of 1.0 mol / l calcium chloride (manufactured by Tomita Pharmaceutical) were added and reacted at 60 ° C. for 24 hours. A phospholipid (phosphatidylcholine) having an acid bonded to the 2-position was obtained. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the oleic acid content was 39.2% by weight.

(Example 2)
To 35 mg of lysophosphatidylcholine (“SLP-LPC70” manufactured by Sakai Oil Co., Ltd.), 113 mg of DHA (manufactured by Tokyo Chemical Industry Co., Ltd.) and 1 g of glycerin (manufactured by Wako Pure Chemical Industries, Ltd.) are added, and 50 mg of glycine (manufactured by Wako Pure Chemical Industries, Ltd.) is further added. Was added. Further, 10 mg of phospholipase A2 (“Lecitase 100S” manufactured by Novozymes Japan, 130 Iu / mg) and 2.5 μl of 1.0 mol / l calcium chloride (manufactured by Wako Pure Chemical Industries, Ltd.) were added, and dibutylhydroxy as an antioxidant. 3 mg of toluene (manufactured by Wako Pure Chemical Industries, Ltd.) was added and reacted at 60 ° C. for 48 hours to obtain a phospholipid (phosphatidylcholine) having a highly unsaturated fatty acid (DHA) bonded to the 2-position. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the DHA content was 34.2% by weight.

Example 3
To 35 mg of lysophosphatidylcholine (SLP-LPC70 manufactured by Sakai Oil Co., Ltd.), 113 mg of DHA (manufactured by Tokyo Chemical Industry Co., Ltd.) and 1 g of glycerin (manufactured by Wako Pure Chemical Industries, Ltd.) are added, and further glycylglycine (manufactured by Wako Pure Chemical Industries, Ltd.) 60 mg Was added. Further, 20 mg of phospholipase A2 (manufactured by Sanyo Fine Co., Ltd., powdered lysonase, 53Iu / mg) and 2.5 μl of 1.2 mol / l calcium chloride (manufactured by Wako Pure Chemical Industries, Ltd.) were added, and sancatel containing catechin as an antioxidant was added. Phospholipid (phosphatidylcholine) in which highly unsaturated fatty acid (DHA) is bonded to the 2-position by adding 3 mg of NO1 (manufactured by Taiyo Kagaku) and 3 mg of ascorbic acid (manufactured by Wako Pure Chemical Industries, Ltd.) and reacting at 60 ° C. for 48 hours. Got. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the DHA content was 30.7% by weight.

Example 4
Polyunsaturated fatty acid (EPA) was bonded to the 2-position in the same manner as in Example 2 except that 104 mg of EPA (manufactured by Nacalai Tesque) was used instead of 113 mg of DHA, and 60 mg of glycine was used instead of 60 mg of glycylglycine. A phospholipid was obtained. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the EPA content was 28.5% by weight.

(Example 5)
The polyunsaturated fatty acid (arachidonic acid) was in the second position in the same manner as in Example 2 except that 103 mg of arachidonic acid (manufactured by Sigma-Aldrich Japan) was used instead of 113 mg of DHA, and 40 mg of glycine was used instead of 60 mg of glycylglycine. A phospholipid (phosphatidylcholine) bound to was obtained. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the arachidonic acid content was 32.3% by weight.

(Example 6)
DHA-containing fatty acid 105 mg prepared by hydrolyzing DHA-50G (manufactured by Nippon Chemical Feed Co., Ltd., containing 51.8% by weight of DHA) in 35 mg of lysophosphatidylcholine (“SLP-LPC70” manufactured by Sakai Oil Co., Ltd.), glycerin (Sakamoto Yakuhin) 1 g of Kogyo Co., Ltd. was added, and 75 mg of glycine (Showa Denko) was further added. Further, 20 mg of phospholipase A2 (“Powder Lysonase” manufactured by Sanyo Fine Co., Ltd.) was added and the water was removed by reducing the pressure at 0.6 torr (80 Pa) for 10 minutes, and then 10 μl of 0.3 mol / l calcium chloride (manufactured by Tomita Pharmaceutical Co., Ltd.) solution. And reacted at 60 ° C. for 48 hours to obtain a phospholipid (phosphatidylcholine) in which a highly unsaturated fatty acid (DHA) was bonded to the 2-position. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the DHA content was 15.5% by weight.

(Example 7)
DHA-containing fatty acid 105 mg prepared by hydrolyzing DHA-50G (manufactured by Nippon Chemical Feed Co., Ltd., containing 51.8% by weight of DHA) in 35 mg of lysophosphatidylcholine (“SLP-LPC70” manufactured by Sakai Oil Co., Ltd.), glycerin (Sakamoto Yakuhin) 1 g of Kogyo Co., Ltd. was added, and 37.5 mg of glycine (manufactured by Showa Denko KK) and 37.5 mg of alanine (manufactured by Musashino Chemical Laboratory) were further added. Further, 20 mg of phospholipase A2 (“Powder Lysonase” manufactured by Sanyo Fine Co., Ltd.) was added and the water was removed by reducing the pressure at 0.6 torr (80 Pa) for 10 minutes, and then 10 μl of 0.3 mol / l calcium chloride (manufactured by Tomita Pharmaceutical Co., Ltd.) solution. And reacted at 60 ° C. for 48 hours to obtain a phospholipid (phosphatidylcholine) in which a highly unsaturated fatty acid (DHA) was bonded to the 2-position. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the DHA content was 17.2% by weight.

(Example 8) Preparation of phospholipid-containing esterification reaction solution for improving phosphatidylcholine purity 35 mg of lysophosphatidylcholine (“SLP-LPC70” manufactured by Sakai Oil Co., Ltd.) and DHA-50G (manufactured by Nippon Chemical Feed Co., Ltd., containing 51.8% by weight of DHA) 30 mg of DHA-containing fatty acid prepared by hydrolyzing the above and 1 g of glycerin (manufactured by Sakamoto Yakuhin Kogyo Co., Ltd.), 37.5 mg of glycine (manufactured by Showa Denko KK) and alanine (manufactured by Musashino Chemical Laboratory) 5 mg was added. Furthermore, 20 mg of phospholipase A2 (“Powder Lysonase” manufactured by Sanyo Fine Co., Ltd.) was added, 6 μl of 0.5 mol / l calcium chloride (manufactured by Tomita Pharmaceutical Co., Ltd.) solution was added, and the water was reduced by reducing the pressure at 0.6 torr (80 Pa) for 10 minutes. The resultant was removed and reacted at 50 ° C. for 24 hours to obtain a phospholipid-containing esterification reaction solution for improving phosphatidylcholine purity. The DHA content in the phospholipid and lysophospholipid contained in the reaction solution was 15.3% by weight.

(Comparative Example 1)
A phospholipid having oleic acid bound to the 2-position was obtained in the same manner as in Example 1 except that glycine was not used. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the oleic acid content was 19.4% by weight.

(Comparative Example 2)
A phospholipid having a highly unsaturated fatty acid (DHA) bound to the 2-position was obtained in the same manner as in Example 3 except that glycylglycine was not used. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the DHA content was 12.9% by weight.

(Comparative Example 3)
A phospholipid having a highly unsaturated fatty acid (EPA) bound to the 2-position was obtained in the same manner as in Example 4 except that 60 μl of water was added without using glycine. In the fatty acid composition of the obtained phospholipid and lysophospholipid, the EPA content was 8.9% by weight.

(Comparative Example 4)
A phospholipid having a highly unsaturated fatty acid (arachidonic acid) bonded to the 2-position was obtained in the same manner as in Example 5 except that glycine was not used. In the fatty acid composition in the obtained phospholipid and lysophospholipid, the arachidonic acid content was 5.5% by weight.

(Comparative Example 5)
A phospholipid having a highly unsaturated fatty acid (DHA) bound to the 2-position was obtained in the same manner as in Example 6 except that glycine was not used. In the fatty acid composition of the obtained phospholipid and in the lysophospholipid, the DHA content was 4.4% by weight.

(Comparative Example 6)
A phospholipid in which a highly unsaturated fatty acid (DHA) was bonded to the 2-position was obtained in the same manner as in Example 8 except that glycine and alanine were not used. In the fatty acid composition of the obtained phospholipid and lysophospholipid, the DHA content was 7.6% by weight.

(Example 9) Acetone extraction The operation of adding 100 μl of acetone to 100 mg of the reaction solution obtained in Example 8 for liquid separation and separating the acetone layer (upper layer) was repeated twice. In addition, 200 μl of chloroform-methanol (v / v = 2: 1) is added to the lower layer separated from the acetone layer, and 300 μl of saturated aqueous sodium chloride solution is added for liquid separation to extract the chloroform-methanol layer (lower layer separated from the acetone layer). did. TLC was performed on the acetone layer (upper layer) and the chloroform-methanol layer (lower layer separated from the acetone layer), respectively, and comprehensive evaluation as an extraction method was also performed. The results are summarized in Table 1.

(Example 10) Ethanol + hexane extraction After adding 50 μl of ethanol to 100 mg of the reaction solution obtained in Example 8 and stirring, 50 μl of hexane was added for liquid separation to separate the hexane layer (upper layer). Repeated times. The lower layer separated from the hexane layer was treated in the same manner as in Example 8, and TLC was performed on the lower layer separated from the hexane layer (upper layer) and the hexane layer, respectively, and an overall evaluation as an extraction method was also performed. The results are summarized in Table 1.

(Example 11) Ethanol + acetone extraction After adding 25 μl of ethanol to 100 mg of the reaction solution obtained in Example 8 and stirring, 75 μl of acetone was added for liquid separation to separate the acetone layer (upper layer). Repeated times. The lower layer separated from the acetone layer was treated in the same manner as in Example 8, and TLC was performed on the acetone layer (upper layer) and the lower layer separated from the acetone layer, respectively, and an overall evaluation as an extraction method was also performed. The results are summarized in Table 1.

(Example 12) Extraction with ethanol + acetone / hexane After adding 100 μl of ethanol to 100 mg of the reaction solution obtained in Example 8 and stirring, a mixed solvent of 50 μl of acetone and 50 μl of hexane was added for liquid separation, and acetone / hexane mixing was performed. The operation of separating the solvent layer (upper layer) was repeated twice. The lower layer separated from the acetone / hexane mixed solvent layer was treated in the same manner as in Example 8, TLC was performed on the upper layer and the lower layer, respectively, and an overall evaluation as an extraction method was also performed. The results are summarized in Table 1.

(Example 13) Ethanol + ethyl acetate extraction To 100 mg of the reaction solution obtained in Example 8, 25 μl of ethanol was added and stirred, and then 75 μl of ethyl acetate was added and separated to separate the ethyl acetate layer (upper layer). The operation was repeated twice. The lower layer separated from the ethyl acetate layer was treated in the same manner as in Example 8, and TLC was performed on the lower layer separated from the ethyl acetate layer (upper layer) and the ethyl acetate layer, respectively, and an overall evaluation as an extraction method was also performed. The results are summarized in Table 1.

(Reference Example 1)
To 100 mg of the reaction solution obtained in Example 8, 100 μl of hexane was added for liquid separation, and the operation of separating the hexane layer (upper layer) was repeated twice. The lower layer separated from the hexane layer was treated in the same manner as in Example 8. TLC was performed on the lower layer separated from the hexane layer (upper layer) and the hexane layer, respectively, and an overall evaluation as an extraction method was also performed. The results are summarized in Table 1.

(Reference Example 2)
The operation of adding 100 μl of ethyl acetate to 100 mg of the reaction solution obtained in Example 8 for liquid separation and separating the ethyl acetate layer (upper layer) was repeated twice. The lower layer separated from the ethyl acetate layer was treated in the same manner as in Example 8. TLC was performed on the lower layer separated from the ethyl acetate layer (upper layer) and the ethyl acetate layer, respectively, and comprehensive evaluation as an extraction method was also performed. The results are summarized in Table 1.

Claims (9)

Phospholipase A2 in the esterification reaction of lysophospholipids and fatty acids by perform the esterification reaction with glycerin, and characterized by amino acid and / or amino acid to the reaction system is added following peptides three residues, said amino acid Is a method for producing phospholipids, which is at least one selected from the group consisting of glycine, alanine, asparagine, glutamine, isoleucine, leucine, serine, threonine, valine, phenylalanine and tyrosine . The method for producing a phospholipid according to claim 1, wherein the peptide comprises a combination of glycine, alanine and serine. The method for producing a phospholipid according to claim 1 or 2 , wherein the esterification reaction is performed at 35 ° C or more and 80 ° C or less. The method for producing phospholipid according to any one of claims 1 to 3 , wherein the lysophospholipid is derived from soybean. After the esterification reaction, a ketone solvent is added to form a glycerol solution layer and a ketone solvent layer, the ketone solvent layer is separated, and then the solvent in the ketone solvent layer is distilled off, and then the fatty acid is removed to remove phospholipids. The method for producing a phospholipid according to any one of claims 1 to 4, wherein: After the esterification reaction, an alcohol having 4 or less carbon atoms is added, and a solvent comprising a hydrocarbon solvent and / or a ketone solvent and / or an ester solvent is further added to form a glycerin solution layer and a solvent layer, and the solvent layer The method for producing a phospholipid according to any one of claims 1 to 4, wherein the phospholipid is obtained by removing the fatty acid and then distilling off the solvent in the solvent layer. The method for producing a phospholipid according to claim 5 or 6 , wherein the ketone solvent is acetone. The method for producing a phospholipid according to claim 6 , wherein the alcohol having 4 or less carbon atoms is ethanol. A reaction system containing lysophospholipid obtained by hydrolyzing the 2-position of phospholipid with phospholipase A2 is mixed with an amino acid and / or a peptide having 3 or less amino acids and a fatty acid, and then lysophospholipid by phospholipase A2 is added. A method of introducing a fatty acid at the 2-position of a phospholipid by carrying out an esterification reaction , wherein the amino acid comprises glycine, alanine, asparagine, glutamine, isoleucine, leucine, serine, threonine, valine, phenylalanine, tyrosine The method which is at least 1 sort chosen from more .