JP2010284116A - Method for producing phospholipid composition - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for efficiently producing a phospholipid composition free from a nitrogen-containing base and highly containing a phospholipid. <P>SOLUTION: The method for producing the phospholipid composition includes reacting lecithin with an extract of a soybean enzyme extracted from a soybean seed having ≤145% water absorption, and having ≥9.0 of the activity ratio of phospholipase D to phospholipase C. <P>COPYRIGHT: (C)2011,JPO&INPIT

Description

  The present invention relates to a method for producing a phospholipid composition containing a high amount of phospholipid not containing a nitrogen-containing base.

  Phospholipids are the main lipids that make up biological membranes, but because they have emulsifying action, antioxidant action, etc., they are widely used as food additives in margarine, milk drinks, ice creams, confectionery and the like. On the other hand, phospholipids such as phosphatidylcholine (PC) and phosphatidylethanolamine (PE) are considered to easily cause coloring and odor generation when heated because the nitrogen-containing compounds that are constituents are unstable to heat. (Patent Document 1). Accordingly, phospholipids that do not contain nitrogenous bases, such as phosphatidic acid (PA), phosphatidylinositol (PI), and the like that are high in content, are useful not only for foods but also for various fields such as pharmaceuticals and cosmetics. It is considered.

  As a method for producing PA, there are known a method of hydrolyzing lecithin with phospholipase D (PL-D) and a method of hydrolyzing by combining PL-D and phospholipase C (PL-C) (patent). Literature 2-4). PL-D is an enzyme that hydrolyzes PC or PE into PA and a nitrogen-containing base, and PL-C is an enzyme that hydrolyzes PI into diglyceride and phosphorylinositol.

  Moreover, the method of manufacturing PA by processing a lecithin with oil seed extracts, such as a soybean, is known (patent documents 5 and 6). By this method, PA can be obtained with high purity.

Japanese Examined Patent Publication No. 7-24548 Japanese Patent Laid-Open No. 3-4795 Japanese Examined Patent Publication No. 6-77509 Japanese Patent Laid-Open No. 4-66091 Japanese Patent Publication No. 6-83639 Japanese Examined Patent Publication No. 6-77507

  The conventional techniques for hydrolyzing lecithin using PL-D and PL-C both use microorganism-derived materials as enzyme sources, which are expensive and are not suitable for industrial production. On the other hand, in the method of treating with an oilseed extract such as soybean, the decomposition rate of PI increases, so the yield of phospholipid itself containing no nitrogen-containing base is lowered. In addition, when extracting phospholipids after treatment, separation may be difficult and workability may deteriorate, resulting in a decrease in yield. Therefore, a method is desired that can efficiently produce a phospholipid that does not contain a nitrogen-containing base with good workability.

  Therefore, an object of the present invention is to provide an efficient method for producing a phospholipid composition containing a high amount of a phospholipid not containing a nitrogen-containing base.

The present inventor examined soybean as an enzyme source in a method of treating lecithin with an enzyme-containing extract (hereinafter referred to as “soy enzyme extract”) extracted from soybean seeds. The extract produces a sticky solid after completion of the lecithin hydrolysis reaction, which provides the separation performance when the phospholipid composition is extracted with a continuous centrifugation step or solvent (hexane) during the production of the phospholipid composition. It was found that the extraction rate of phospholipids in the phospholipid composition was lowered as a result. In order to increase the yield of phospholipids not containing nitrogenous bases and to lower the composition ratio of PC and PE, the balance of the activities of PL-D and PL-C in soybean enzyme extract (PL- (D / PL-C activity ratio) was found to be important.
Then, if soybean seeds having a specific water absorption rate are used as soybean as the enzyme source and the activity ratio in the soybean enzyme extract is 9.0 or more, high purity PA can be obtained by decomposing PC and PE. It has been found that the decomposition of PI can be suppressed, the workability is good, and the extraction rate is improved, so that a phospholipid composition containing a high amount of phospholipid not containing a nitrogen-containing base can be produced very efficiently. It was.

  That is, the present invention relates to a phospholipid composition obtained by reacting lecithin with a soybean enzyme extract extracted from soybean seeds having a water absorption of 145% or less and having an activity ratio of phospholipase D and phospholipase C of 9.0 or more. A manufacturing method is provided.

  According to the method of the present invention, it is possible to leave a large amount of PI while decomposing PC and PE, and because the workability is good and the extraction rate is improved, the phospholipid containing no nitrogenous base is highly contained. A phospholipid composition can be obtained efficiently.

  The lecithin used in the present invention is a phospholipid mixture comprising PC, PE, PA, PI, phosphatidylserine (PS) and phosphatidylglycerol (PG), or their lyso form. As lecithin, those derived from various animals and plants and those obtained by chemical synthesis can be used. Naturally derived lecithin made from soybeans, egg yolks and the like is preferred. Also, paste-like crude lecithin, defatted lecithin from which oils and fats have been removed, hydrogenated lecithin, and the like can be used.

The soybean seed used in the present invention has a water absorption of 145% or less. When an enzyme extract obtained from soybean seeds having a water absorption rate exceeding 145% is used, a viscous solid is produced after the hydrolysis reaction of lecithin. In this case, the separability, that is, the workability is remarkably poor, and the extraction rate is poor. In addition, when an enzyme extract obtained from soybean seeds having a water absorption rate of 145% or less is used, PI also has a characteristic that PI is more difficult to be decomposed. The water absorption rate of soybean seeds is further preferably 100 to 140%, particularly preferably 120 to 139% from the viewpoints of workability, extraction rate, and difficulty in decomposing PI. The water absorption rate of soybean seeds can be determined by immersing the soybean seeds in 10 times the weight of water for 20 hours and calculating the ratio of the soybean mass after immersion to the soybean mass before immersion (the following formula [1]).
Water absorption (%) = {(Soybean mass after immersion (g) −Soybean mass before immersion (g)) / Soybean mass before immersion (g)} × 100 [1]

  The soybean enzyme extract can be obtained by extracting soybean seeds raw or dried and then crushed. In the present invention, it is preferable to use normal dried soybeans that have been dried so that they can be stored for a long time. The crushing process is not particularly limited, and can be performed by a known apparatus and method such as a Waring blender. After the crushing treatment, a material obtained by sieving to remove impurities may be used.

  The extraction method may be any of immersion, decoction, leaching, reflux extraction, column flow extraction, supercritical extraction, ultrasonic extraction, microwave extraction, and the like. For the extraction, for example, column extraction is preferably performed from the viewpoint of maintaining enzyme activity.

Examples of the extract include water or an aqueous solution containing one or more of alkali metal salts or alkaline earth metal salts. Examples of the alkali metal salt or alkaline earth metal salt include alkali metal or alkaline earth metal carboxylates, phosphates, carbonates; alkali metal or alkaline earth metal halides, hydroxides, and the like. It is done. Of these, carboxylates, phosphates and halides are preferred. These can be used alone or in combination of two or more.
Examples of the carboxylic acid include linear or branched aliphatic carboxylic acids having 2 to 8 carbon atoms, dicarboxylic acids, tricarboxylic acids, and aromatic carboxylic acids having 7 to 12 carbon atoms, such as acetic acid, butyric acid, and propionic acid. Succinic acid, citric acid, benzoic acid and the like. Examples of the alkali metal include sodium and potassium, and examples of the alkaline earth metal include magnesium and calcium.

  The extract preferably has a buffer capacity. Examples of the buffering ability include sodium acetate buffer, sodium citrate buffer, sodium phosphate buffer, sodium citrate-sodium acetate buffer, and the like. Further, these buffer solutions may be used in combination with, for example, alkali metal or alkaline earth metal halides that do not have buffer capacity.

  When using an aqueous solution containing an alkali metal or alkaline earth metal carboxylate or phosphate as the extract, the concentration of the carboxylate or phosphate ions in the extract maintains the enzyme activity efficiently. Therefore, the range of 0.05 to 1.0M, particularly 0.1 to 0.5M is preferable.

  The pH of the extract is preferably in the range of pH 4 to 7.5, particularly pH 5 to 7 from the viewpoint of extraction efficiency.

  The obtained soybean enzyme extract is added with stabilizers such as sugars, proteins, various salts as necessary, and is made into a liquid or solid form by treatment such as concentration under reduced pressure, drying or freeze-drying. The above extract can be added and used. The soybean enzyme extract may be a crude product as long as it exhibits the effects of the present invention, and the obtained crude product is combined with known separation and purification methods as appropriate to increase the purity thereof. May be. Examples of the purification means include organic solvent precipitation, centrifugation, ultrafiltration membrane, high performance liquid chromatograph, column chromatograph and the like.

  In the present invention, the activity ratio (PL-D / PL-C activity ratio) of phospholipase D (PL-D) and phospholipase C (PL-C) in the soybean enzyme extract is 9.0 or more. By using a soybean enzyme extract having a PL-D / PL-C activity ratio of 9.0 or more, the PA composition ratio of the phospholipid composition is increased, while the degradation rate of PI can be suppressed. The content of phospholipids that do not contain a nitrogen-containing base in the phospholipid composition can be improved. The PL-D / PL-C activity ratio is preferably 9.0 to 15.0, more preferably 10.2 to 13.0, and particularly preferably 10.5 to 12.0.

  In the present invention, the reaction between lecithin and the soybean enzyme extract is preferably carried out at a reaction temperature of 10 to 60 ° C., preferably 20 to 50 ° C. from the viewpoint of reaction efficiency, by mixing and stirring them into a slurry. The use ratio of the soybean enzyme extract is 1 to 50, preferably 1 to 10 in terms of mass ratio with respect to lecithin. Moreover, it is preferable to carry out in presence of inert gas, such as nitrogen and argon, so that contact with air may be avoided as much as possible.

  Moreover, in order to further increase the content of phospholipids that do not contain a nitrogenous base in the phospholipid composition, the composition ratio of each phospholipid (mass% in the total phospholipid mass) is measured over time, The reaction is preferably terminated when the PA composition ratio of the phospholipid reaches 90% or more. After completion of the reaction, it is preferable that the solid content is separated from the reaction solution by centrifugation or the like, washed with water, and then extracted with an organic solvent such as hexane and purified. The phospholipid composition after extraction with an organic solvent contains diacylglycerol produced by decomposing PI in addition to phospholipid, and the content depends on the decomposition rate of PI. It is about 5-15 mass% in a composition.

  Thus, the PA composition ratio of the phospholipid in the phospholipid composition is 90% or more, preferably 90 to less than 96%, more preferably less than 90 to 94%, and the PA degradation rate is 80% while being obtained with high purity. Less than, preferably less than 66%, more preferably not less than 60% and less than 66%, and a phospholipid containing no nitrogen-containing base can be obtained efficiently. The PI composition ratio of the phospholipid in the phospholipid composition is 4% or more, preferably 5% or more and less than 10%.

  Further, the composition ratio of phospholipids (PA and PI) not containing a nitrogen-containing base of phospholipid in the phospholipid composition is preferably 94% or more, more preferably 96% or more, and particularly preferably 97 to 99.5%. The composition ratio of phospholipid PC and PE in the phospholipid composition is preferably less than 6%, more preferably less than 5%, and particularly preferably less than 3%. Furthermore, the total composition ratio of phospholipids other than these, such as phosphatidylserine, is preferably 0.5% or less, particularly preferably 0.1% or less.

[Analysis method]
(1) PL-C activity measurement method PL-C activity here means the amount (nmol) of PI that 1 ml of soybean enzyme extract hydrolyzes in 1 minute. PI is converted to inositol phosphate by PL-C. After the step of decomposing into diacylglycerol, the amount of inositol phosphate produced was measured by the following method.
<Reagent>
(A) Substrate / buffer solution: 80 mg of PI (SIGMA P-6636) as a substrate was added to 5 ml of 0.5% deoxycholic acid (Tokyo Chemical Industry) aqueous solution, and 10 ml of 0.38 M acetic acid buffer (pH 6) was further dissolved.
(B) Phosphorus standard solution: A solution obtained by dissolving monopotassium phosphate (Wako Pure Chemical Industries, Ltd.) with distilled water so that the phosphorus content is accurately 0.5 mM.
(C) Reaction stop solution: Mixture of 66 ml of chloroform, 33 ml of methanol and 1 ml of concentrated hydrochloric acid.
(D) Oxidizing agent
(E) Decolorizer
(F) Color former
(D) to (F) used a phospholipid test kit reagent (manufactured by Wako Pure Chemical Industries, Ltd.) of permanganate ashing method.
<Operation>
(i) 100 μL of a sample to be measured (soy enzyme extract obtained by “Preparation of soybean enzyme extract” below) was accurately measured in a test tube. At this time, the test tube which does not take a sample as a blank was prepared and analyzed simultaneously.
(ii) In a 37 ° C. water bath, 400 μL of the substrate / buffer solution of (A) was accurately weighed into each of the two test tubes, added and mixed, and allowed to stand for 30 minutes after the addition.
(iii) At the same time, 500 μL of distilled water as a standard blank and 500 μL of the phosphorus standard solution (B) as standard phosphorus were accurately measured in a test tube for preparing a calibration curve.
(iv) Accurately add 2.5 mL of the reaction stop solution of (C) above to each test tube containing the sample and blank of (i) and the standard blank and phosphorus standard solution for preparation of the calibration curve of (iii), Mix well.
(v) The above test tube was directly centrifuged at 1000 rpm for 10 minutes, and 200 μL of the upper layer was accurately weighed into another test tube.
(vi) 0.2 mL of sulfuric acid was accurately added to a test tube from which the upper layer was collected by centrifugation, mixed, and then left in a boiling bath for 10 minutes.
(vii) After accurately adding 1.0 mL of the oxidizing agent (D) and mixing, a glass ball was placed on the test tube and left in a boiling bath for 30 minutes.
(viii) The mixture was allowed to cool at room temperature for 10 minutes, and a glass ball was taken out.
(ix) 1.0 mL of the decoloring agent (E) was added accurately and stirred well.
(x) The color developing agent (F) (0.25 mL) was accurately added and mixed, and then left in a 37 ° C. water bath for 20 minutes.
(xi) Cooled with running water for 10 minutes.
(xii) Absorbance at 660 nm was measured with an absorptiometer (HITACHI, U-3310), and activity was determined from the following formula [2].

  Activity (nmoL / min · mL) = (Sample Absorbance−Blank Absorbance) × 83.3 / (Standard Phosphorus Absorbance−Standard Blank Absorbance) [2]

(2) PL-D activity measurement method PL-D activity here means the amount (nmol) of PC that 1 ml of soybean enzyme extract hydrolyzes in 1 minute. After the step of decomposing, the produced choline was measured by the following method of measuring by choline oxidase / phenol method.
<Reagent>
(G) Substrate / buffer solution: 0.3 g of PC (trade name Epicron S-200, manufactured by Lucas Mayer) as a substrate, 10 ml of 0.13% nonidet P-40 (SIGMA N-3516) aqueous solution and 75 mM acetate buffer (75 mM chloride) Calcium containing; pH 6.0) 20ml added and dissolved.
(H) Standard choline chloride solution: 50 mM acetate buffer solution (containing 50 mM calcium chloride; pH 6.0) containing 0.2 mM choline chloride (SIGMA C-1879)
(I) Reaction stop solution: 1 M Tris-HCl buffer (containing 150 mM EDTA2 sodium dihydrate; pH 8.0).
(J) Chromogenic substrate solution: A solution prepared by dissolving 61 mg of 4-aminoantipyrine in 100 ml of 100 mM Tris-HCl buffer (containing 4 mM phenol; pH 8.0).
(K) Coloring solution: A solution obtained by dissolving 6 mg of choline oxidase (SIGMA C-5896) and 1 mg of peroxidase (Wako Pure Chemical Industries) in 10 ml of the above (J) coloring substrate solution.
(L) Color stop solution: 1% (w / v) Triton X-100 (Wako Pure Chemical Industries) aqueous solution.
<Operation>
(i) 200 μL of a sample to be measured (soy enzyme extract obtained by “Preparation of soybean enzyme extract” below) diluted 50 times with 75 mM acetate buffer was accurately taken in a test tube. At this time, prepare a test tube that does not take a sample as a blank, a test tube that accurately takes 200 μL of distilled water as a standard blank, and a test tube that accurately takes 200 μL of the (H) standard choline chloride solution as a standard choline, Analyzed simultaneously.
(ii) In a 37 ° C. water bath, 300 μL of the (G) substrate / buffer solution was accurately added to each test tube, mixed, and allowed to stand for 10 minutes after the addition.
(iii) After exactly 10 minutes, 200 μL of the (I) reaction stop solution was accurately added to each test tube and mixed well.
(iv) The above (K) coloring solution (500 μL) was accurately added to each test tube, mixed, and allowed to stand in a 37 ° C. water bath for 20 minutes for color development.
(v) Add exactly 2 mL of the (L) color stop solution to each test tube, mix, measure the absorbance at 500 nm with an absorptiometer (HITACHI, U-3310), and determine the activity from the following formula [3]. It was.

  Activity (nmoL / min · mL) = 20 × (sample absorbance−blank absorbance) × (sample dilution factor) / (standard choline chloride absorbance−standard blank absorbance) [3]

(3) Method for measuring phospholipid composition Hexane was added in a ratio of 3 mL to 1 mL of the phospholipid composition and mixed well. The mixture was centrifuged at 3000 rpm for 10 minutes, and the upper layer was collected. 1 mL of chloroform was added to 3 to 4 drops of the obtained upper layer. 10 μL of this solution was injected into a liquid chromatograph, and the phospholipid composition was determined from the following formula [4].
Liquid chromatographic measurement column: Wakosil NH2 (5μm), 4.0 × 150mm (Wako Pure Chemical Industries)
Column temperature: 40 ° C
Eluent: acetonitrile / ethanol / 12mM ammonium dihydrogen phosphate aqueous solution (30/65/5 volume ratio)
Flow rate: 1.0ml / min
Detection: UV 210nm

  Molar composition ratio (%) of each phospholipid = peak area of each phospholipid / sum of peak areas of four component phospholipids (PC, PE, PA, PI) [4]

Examples 1-6, Comparative Examples 1 and 2
(1) Preparation of soybean enzyme extract Six types of commercially available dried soybeans (200 g) were each crushed with a Waring blender. The crushed material is sieved to remove contaminants, then packed into a glass column, and the extract (0.4 M sodium acetate buffer containing 50 mM calcium chloride; pH 6.) adjusted from the bottom of the column while adjusting the flow rate to 3.3 ml / min with a peristaltic pump. 0) and 900 g of enzyme extract was recovered from the top of the column.
(2) Enzymatic reaction In a 1000 mL four-necked flask equipped with a stirrer, 100 g of commercially available defatted lecithin (trade name SLP-WSP: manufactured by Sakai Oil Co., Ltd.) is added, and 600 g of enzyme extract is added to this, and the light is blocked The reaction was performed at 30 ° C. in a nitrogen gas atmosphere. The lecithin contained 100% by mass of phospholipid, and the phospholipid composition (molar ratio) was PA 10.9%, PI 16.2%, PC 38.2%, PE 34.7%. When the molar ratio of PA in the phospholipid reached 90% (Examples 1 to 4, Comparative Examples 1 and 2), and when the molar ratio of PA further increased (Examples 5 and 6), The phospholipid composition was collected and analyzed by high performance liquid chromatography. The total phospholipid yield (calculated value of the total phospholipid mass), PA + PI yield and each yield after the reaction were shown below. Obtained according to the calculation.
(3) Calculation method Since the raw material lecithin before starting the reaction is composed of PA, PC, PE and PI, the mass of each phospholipid in 100 g of the raw material lecithin is the number of moles of each phospholipid in the average molecular weight. It can be calculated by multiplying. Here, since the number of moles of each phospholipid in the raw lecithin is a value proportional to the molar composition ratio, the molar composition ratios of PA, PC, PE and PI in the raw lecithin are respectively A, B, C. And D, and the average molecular weights of Mw _PA , Mw _PC , Mw _PE and Mw _PI , for example, the mass W _PA of PA in 100 g of raw lecithin is:
W _PA = {(Mw _PA × A) / (Mw _PA × A + Mw _PC × B + Mw _PE × C + Mw _PI × D)} × 100
Therefore, the molar number Mn _PA of PA in 100 g of raw material lecithin is
Mn _PA = W _PA / Mw _PA
It is. Similarly, Mn _PC , Mn _PE and Mn _PI are calculated for other phospholipids.
Next, the number of moles of each phospholipid after the reaction is mn _PA , mn _PC , mn _PE , mn _PI , and the molar composition ratio of PA, PC, PE and PI after the reaction is a, b, c and d, respectively. And Here, PI is decomposed into DAG by the reaction and decreases. However, since PC and PE each generate PA by the enzymatic reaction, the total number of moles of PA + PC + PE does not change before and after the reaction.
mn _PA + mn _PC + mn _PE = Mn _PA + Mn _PC + Mn _PE
And therefore
mn _PI / (Mn _PA + Mn _PC + Mn _PE + mn _PI ) = d
Here, if Mn _PA + Mn _PC + Mn _PE = X, the following formula is derived.
mn _PI = d × X / (1-d)
Then, the number of moles of PA, PC and PE after completion of the reaction is respectively
mn _PA = a × {X + d × X / (1-d)}
mn _PC = b × {X + d × X / (1-d)}
mn _PE = c × {X + d × X / (1-d)}
It becomes. From the above, the yield was calculated by multiplying the number of moles of each phospholipid after the reaction by the respective average molecular weight, and the “total phospholipid yield” and “PA + PI yield” were determined.
Moreover, the decomposition rate of PI was calculated from the following formula [5], and the yield of diacylglycerol (DAG) produced by the decomposition of PI was calculated from the following formula [6].
Decomposition rate of PI (%) = (Mn _PI −mn _PI ) / Mn _PI × 100 [5]
Yield of DAG = (Mn _PI −mn _PI ) × average molecular weight of DAG [6]
The water absorption rate of soybean was calculated from the above formula [1].

After completion of the reaction, the solid content obtained by centrifuging the reaction solution (3000 rpm × 10 minutes) is subjected to a water washing step by repeating water addition (500% of 1% NaCl aqueous solution) and centrifugation (four times). It was suspended in 700 ml of hexane (Hex) in a liquid funnel, and the phospholipid composition was extracted. The separation phase of the Hex phase and the aqueous phase was observed after 30 minutes of stirring in the separatory funnel, and the separability when extracting the phospholipid composition with Hex was evaluated according to the following criteria.
[Separability]
○: The state where the interface between the Hex phase and the aqueous phase is completely separated after 30 minutes of stirring and standing Δ: The state where the interface between the Hex phase and the aqueous phase is completely separated after 60 minutes of stirring and standing x: More than 60 minutes when standing still A state in which the interface between the Hex phase and the aqueous phase does not separate even after elapse

Furthermore, the actual value of the final yield of the phospholipid composition after removing Hex from the phospholipid composition obtained after extraction with Hex, and the yield of the phospholipid composition containing total phospholipid and diacylglycerol after the reaction was completed. The extraction rate was calculated from the calculated value by the following formula [7].
Extraction rate (%) = actual value of final yield of phospholipid composition after removal of Hex (g) / calculated value of yield of phospholipid composition after completion of reaction (g) × 100 [7]
The results are shown in Table 1.

From the results shown in Table 1, a soybean enzyme extract extracted from soybean seeds having a water absorption of 145% or less and having an activity ratio of PL-D and PL-C of 9.0 or more is added to lecithin for reaction. Thus, it was confirmed that a phospholipid composition containing a high concentration of a phospholipid not containing a nitrogen-containing base can be efficiently produced.
That is, in Example 1-6, the PC and PE decomposition rates were high, the PI decomposition rate could be suppressed, and the phase separation state of the reaction solution was good, so the separability when extracting the phospholipid composition The yield of PA + PI was good. On the other hand, in Comparative Example 1 using the soybean enzyme extract in which the activity ratio of PL-D and PL-C is less than 9.0, the PI degradation rate becomes extremely high and does not contain the nitrogenous base in the phospholipid composition. The yield of phospholipid was poor.
In Comparative Example 2 where the water absorption rate of soybean seeds exceeds 145%, the PI decomposition rate is high, and the phase separation state of the reaction solution is inferior and the separability is extremely low. Therefore, phosphorus containing no nitrogenous base in the phospholipid composition is contained. The yield of lipid was poor.

Claims (5)

  A method for producing a phospholipid composition comprising reacting lecithin with a soybean enzyme extract extracted from soybean seeds having a water absorption of 145% or less and having an activity ratio of phospholipase D and phospholipase C of 9.0 or more.   The method according to claim 1, wherein the lecithin is naturally derived lecithin.   The production method according to claim 1 or 2, wherein, among the phospholipids in the phospholipid composition, the composition ratio of phospholipids not containing a nitrogenous base is 94% or more.   The production method according to claim 3, wherein the phospholipids not containing a nitrogen-containing base are phosphatidic acid and phosphatidylinositol.   The production method according to any one of claims 1 to 4, wherein the phosphatidic acid composition ratio is 90% or more and the phosphatidylinositol composition ratio is 4% or more among the phospholipids in the phospholipid composition.