JPS6130555B2 - - Google Patents

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Publication number
JPS6130555B2
JPS6130555B2 JP53071517A JP7151778A JPS6130555B2 JP S6130555 B2 JPS6130555 B2 JP S6130555B2 JP 53071517 A JP53071517 A JP 53071517A JP 7151778 A JP7151778 A JP 7151778A JP S6130555 B2 JPS6130555 B2 JP S6130555B2
Authority
JP
Japan
Prior art keywords
lysolecithin
reaction
pancreatin
lecithin
egg yolk
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP53071517A
Other languages
Japanese (ja)
Other versions
JPS55315A (en
Inventor
Hiroshi Kodama
Masao Nakabayashi
Yoshifumi Nakajima
Zenzo Mihashi
Takashi Nagai
Isao Myokan
Tetsuya Kajita
Takashi Sano
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyama Chemical Co Ltd
Original Assignee
Toyama Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyama Chemical Co Ltd filed Critical Toyama Chemical Co Ltd
Priority to JP7151778A priority Critical patent/JPS55315A/en
Publication of JPS55315A publication Critical patent/JPS55315A/en
Publication of JPS6130555B2 publication Critical patent/JPS6130555B2/ja
Granted legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)

Description

【発明の詳細な説明】 本発明は、牛脳、豚脳、鶏卵黄または大豆ホモ
ジネートに、豚すい臓抽出酵素パンクレアチンを
作用させ、反応後、加熱処理することを特徴とす
る天然型リゾレシチン(リゾホスフアチジルコリ
ン)の製造法に関する。
Detailed Description of the Invention The present invention provides natural lysolecithin (lysolecithin), which is characterized by reacting bovine brain, pig brain, chicken egg yolk, or soybean homogenate with pancreatin, an enzyme extracted from pig pancreas, and heat-treating it after the reaction. phosphatidylcholine).

従来、リゾレシチン類は免疫賦活作用及び平滑
筋の収縮に対する抑制作用等の有用な性質を有
し、この化合物にはα型及びβ型の構が存在する
とが知られている。そして天然型リゾレシチンの
製造法として、次に示す方法が知られている。
It has been known that lysolecithins have useful properties such as immunostimulatory effects and inhibitory effects on smooth muscle contraction, and that these compounds have α-type and β-type structures. The following method is known as a method for producing natural lysolecithin.

(i) 天然型レシチンを原料として、ダ毒ホスホリ
パーゼで処理することによりリゾレシチンを得
る方法。〔アンセル、ジイー・ビーおよびハウ
トーム、ジエー・エヌ(Ansell,G.B &
Howthome,J.N.),1964“ホスホリピド
(phospholipids)”,アムステルダム
(Amsterdam),95:エルサリア(Elserier)〕 (ii) 天然型レシチン(試薬レシチン)を原料とし
て、パンクレアチンで処理することによりリゾ
レシチンを得る方法。デイ・ジー・ハナハン
(D.J.Hanahan),ジヤーナル オブ バイオロ
ジカル・ケミストリー(J.Biol.Chem.)第195
巻、第199頁(1952)〕 しかし、上記方法において(i)では、用いるダ毒
ホスホリパーゼAが、非常に高価でかつ皮膚侵食
性を有し取り扱いが困難であり、また反応後の操
作も繁雑であるという欠点を有しており、また(ii)
では、用いる市販レシチンが大豆又は卵より抽出
分離したものであるが、その組成は極めて悪く、
本発明の原料となるレシチン含量は少なく高純度
のレシチンを得ようとする時は、非常に高価とな
る。またたとえば高純度のレシチンを用いたとし
ても、レシチン自体の不飽和脂肪残基が相当量酸
化されているため、パンクレアチンの活性が著し
く低下し、パンクレアチンによる脱アシル化にお
ける反応速度が非常に遅くなり、反応完結まで長
時間を要するなどの欠点がある。さらに、反応終
了後の操作において、市販レシチンを原料として
使用した場合、反応液は乳化状態となり、その後
の単離精製は、フオルヒ(Folch)分配及びカラ
ムクロマトグラフイー等の手段を用いなければな
らず非常に繁雑であるなどの欠点を有する。
(i) A method for obtaining lysolecithin by using natural lecithin as a raw material and treating it with datoxin phospholipase. [Ansell, GB &
Howthome, JN), 1964 “Phospholipids”, Amsterdam, 95: Elserier] (ii) A method for obtaining lysolecithin by treating natural lecithin (reagent lecithin) with pancreatin. . DJ Hanahan, Journal of Biological Chemistry (J.Biol.Chem.) No. 195
Vol., p. 199 (1952)] However, in the above method (i), the datoxin phospholipase A used is very expensive and erosive to the skin, making it difficult to handle, and post-reaction operations are also complicated. (ii)
The commercially available lecithin used is extracted and separated from soybeans or eggs, but its composition is extremely poor.
Lecithin, which is a raw material for the present invention, has a low content and is very expensive if high purity lecithin is to be obtained. Furthermore, even if highly purified lecithin is used, a considerable amount of unsaturated fat residues in lecithin itself are oxidized, which significantly reduces the activity of pancreatin and significantly slows down the reaction rate of pancreatin-induced deacylation. It has disadvantages such as being slow and requiring a long time to complete the reaction. Furthermore, when commercially available lecithin is used as a raw material in the operation after the completion of the reaction, the reaction solution becomes an emulsified state, and subsequent isolation and purification must be performed using methods such as Folch partitioning and column chromatography. However, it has drawbacks such as being extremely complicated.

従つて上記のことから、方法(i)及び(ii)はいずれ
も、工業的製造法としては不向きである。
Therefore, from the above, both methods (i) and (ii) are unsuitable as industrial production methods.

本発明者等は、パンクレアチンを作用させ、レ
シチンよりリゾレシチンを工業的に容易に得る方
法について鋭意研究した結果、動植物の新鮮なレ
シチン含有組織、即ち、豚脳、牛脳、大豆、特に
鶏卵黄そのものを用いた場合はパンクレアチンの
酵素分解反応に於いて、その組織に含まれる補酵
素により相乗効果の結果、脱アシル化反応が非常
に円滑に進行すると共に、好収率で目的とするリ
ゾレシチンが生成することも見出した。また、反
応液に蛋白質及びオリゴペプチド等が含有されて
いることから、、フオルヒ((Folch)分配及びカ
ラムクロマトグラフイー等の操作でリゾレシチン
を単離するとは困難であがが、反応後加熱処理、
特に50〜120℃に加熱する蛋白質の熱変性工程を
導入するとにより、驚くべきことに変性を受けた
凝固蛋白質中に、定量的に目的とするリゾレシチ
ンが吸着され、その後、溶媒抽出等の操作により
容易に分離できる利点を有する。
As a result of intensive research on a method for industrially obtaining lysolecithin from lecithin by applying pancreatin, the present inventors found that it is possible to obtain lysolecithin from fresh lecithin-containing tissues of animals and plants, namely pig brain, cow brain, soybean, and especially chicken egg yolk. When used as such, in the enzymatic decomposition reaction of pancreatin, as a result of the synergistic effect of the coenzyme contained in the tissue, the deacylation reaction proceeds very smoothly, and the desired lysolecithin is produced in a high yield. was also found to be generated. In addition, since the reaction solution contains proteins, oligopeptides, etc., it is difficult to isolate lysolecithin using operations such as Folch partitioning and column chromatography, but post-reaction heat treatment ,
In particular, by introducing a thermal denaturation process for proteins heated to 50 to 120°C, surprisingly, the target lysolecithin is adsorbed quantitatively into the denatured coagulated proteins, and then through operations such as solvent extraction, It has the advantage of being easily separated.

本発明方法は上記知見に基づき完成されれたも
のであつて、天然型リゾレシチンの工業的製造法
として極めて優れた方法である。
The method of the present invention has been completed based on the above findings, and is an extremely excellent method for industrially producing natural lysolecithin.

以下さらに本発明を詳細に説明する。 The present invention will be further explained in detail below.

本発明を実施するにあたり、市販パンクレアチ
ン中には反応に必要なホスホリパーゼA2以外
に、少量のホスホリパーゼA1も存在ていると考
えられるが、一般に、この考素による影響はほと
んどないため、ホスホリパーゼA1の活性を失活
させるための加熱処理を、前もつて行なう必要は
ない。本発明方法は、まず牛脳、豚脳、鶏卵黄ま
たは大豆ホモジネートにパンクレアチンを添加
し、水中で反応させるのであるが、一般的によく
知られているように、使用するパンクレアチンに
含まれている前記以外の酵素、例えば、リボヌク
レアーゼ、アミラーゼ、トリプシン、キモトリプ
シン、リパーゼ並びにカルボキシペプチターゼA
及びB等の活性を抑制させるために、反応系に塩
化カルシウム及びデオキシコール酸を添加するの
が好ましい。そして上記反応は、一般に5〜50
℃、好ましくは35℃でPH7.0〜8.0の条件で行なわ
れ、一般に30分〜12時間で反応は終了する。例え
ば、原料として鶏卵黄を用いる場合、鶏卵黄1個
(18―20g)あたり0.1〜2.0gのパンクレアチンを
使用すると、約3時間で反応は終了する。反応
後、反応液は乳濁状態であるが、その大部分は蛋
白質と脂肪酸である。この反応液を100〜120℃で
加熱処理することより蛋白質を凝固させ、目的物
をその中に吸着させる。この凝固蛋白質を取
し、以下常法の手段を利用するとにより、目的物
を単離採取することができる。例えば、上記で得
られる凝固蛋白質を、メタノール、エタノール、
イソプロパノール等のアルコール類等に懸濁さ
せ、不溶蛋白質を除去し、得られる抽出溶液から
溶媒を減圧下に留去し、残渣にハロゲン化炭化水
素類、アルコール類及び水の混合溶媒を加え、有
機層を分取する。そして減圧下に溶媒を留去し、
更に脂肪酸、中性脂肪スフインゴミエリン及びオ
リゴペプチド類を除去するために、メタノール、
エタノール等のアルコール類及びn―ヘキサン又
はシクロヘキサン等の炭化水素系溶媒で抽出処理
を行なつた後、プロパノール及びエタノール等の
アルコール類で溶媒分離すれば、容易に高純度の
リゾレシチンを得るとができる。
In carrying out the present invention, in addition to the phospholipase A 2 necessary for the reaction, it is thought that a small amount of phospholipase A 1 is also present in commercially available pancreatin, but in general, this consideration has little effect, so phospholipase There is no need to perform a heat treatment in advance to deactivate the activity of A1 . In the method of the present invention, pancreatin is first added to cow brain, pig brain, chicken egg yolk, or soybean homogenate and reacted in water. Enzymes other than those mentioned above, such as ribonuclease, amylase, trypsin, chymotrypsin, lipase, and carboxypeptidase A
In order to suppress the activities of B and B, it is preferable to add calcium chloride and deoxycholic acid to the reaction system. And the above reaction is generally 5 to 50
The reaction is carried out at a temperature of 35°C, preferably 35°C, and a pH of 7.0 to 8.0, and the reaction is generally completed in 30 minutes to 12 hours. For example, when chicken egg yolk is used as a raw material and 0.1 to 2.0 g of pancreatin is used per chicken egg yolk (18 to 20 g), the reaction is completed in about 3 hours. After the reaction, the reaction solution is in a milky state, mostly consisting of proteins and fatty acids. By heating this reaction solution at 100 to 120°C, the protein is coagulated and the target substance is adsorbed therein. The target product can be isolated and collected by taking this coagulated protein and using conventional methods. For example, the coagulation protein obtained above can be mixed with methanol, ethanol,
Suspend in alcohol such as isopropanol to remove insoluble proteins, remove the solvent from the resulting extraction solution under reduced pressure, add a mixed solvent of halogenated hydrocarbons, alcohol, and water to the residue, and add organic Separate the layers. Then, the solvent was distilled off under reduced pressure.
Furthermore, in order to remove fatty acids, neutral fat sphingomyelin and oligopeptides, methanol,
Highly purified lysolecithin can be easily obtained by performing an extraction process with an alcohol such as ethanol and a hydrocarbon solvent such as n-hexane or cyclohexane, followed by solvent separation with an alcohol such as propanol and ethanol. .

次に実施例を挙げて本発明を説明する。 Next, the present invention will be explained with reference to Examples.

実施例 1 市販の鶏卵100個から卵黄のみを分取し、蒸留
水2.5に分散させる。あらかじめ、塩化カルシ
ウム二水塩4.4gを蒸留水200mlに溶解させたも
の、デオキシコール酸ナトリウム5.0gを蒸留水
200mlに溶解させたもの、及びパンクレアチン
(和光純薬製)100gを蒸留水200mlを懸濁させて
おいたものを、上記分散液中に添加し、30〜35℃
で3時間攬拌する。次に、反応液を塩化カルシウ
ムを溶かした水浴上で105〜110℃で3時間加熱す
る。放冷後、遠心脱水を行なつて、1.1Kgの黄褐
色物質を得る。これにメタノール1.2を加え、
室温下で30分間攬拌後、不溶物をロ別する。更に
これにメタノール1.6,1.6,1.0を加え、抽出を
くり返し、抽出液を集めて常圧下で2まで濃縮
させる。次いでクロロホルム2と水1を加
え、クロロホルム層を分取する。さらに水層にク
ロロホルムを400ml加えてクロロホルム層を分取
し、得られたクロロホルム溶液をあわせて減圧下
に溶媒を留去し480gの褐色物質を得る。(この褐
色物質を、粗製物1とする。) 次に、この粗製物1に80%メタノール水溶液1
及びn―ヘキサン400mlを加え、下層を分取
し、更に上層溶液に80%メタノール水溶液500ml
を加え、下層を分取する。得られたメタノール水
溶液をあわせて減圧下に溶媒を留去する。残渣に
エタノール200mlを加え、不溶物をロ別しロ液か
ら減圧下に溶媒を留去し、続いてイソプロパノー
ル200mlを加え、不溶物をロ別する。ロ液から減
圧下に溶媒を留去し、更にトルエンと共沸させる
ことにより脱水処理を行なえば淡黄色物質133g
を得る。これをピリジン及びエタノールからそれ
ぞれ1回ずつ再結晶すれば白色無定形晶状のリゾ
レシチン29gを得る。(尚、鶏卵黄1個中には、
レシチンが500〜700mg含まれているといれてい
ることから鶏卵黄1個に600mlのレシチンが含ま
れているとすれば、本実施例の収率は71.4%であ
る。) IR(KBr)cm-1 1720,1460,1235, 1080,1050,960 NMR(CDC18)τ値 6.10(9H)6.80(9H) 7.65(2H)8.70(27H) 9.10(3H) 旋光度 〔α〕20/D=−2.75(C=11.5,CHC13
CH3 OH=4:1) 〔α〕20/D=−0.66(C=10.6,CHC13
CH3 OH=1:1) 実施例 2 実施例1で得られた粗製物1480gに、ピリジ
ン800mlを加え加熱溶解させる。一晩放置後、析
出している結晶をロ取し、これにエタノール200
mlを加えた後、不溶物をロ別し、ロ液にエーテル
500mlをすばやく加えると、白色結晶37gが析出
してくる。これをロ取し、ピリジン及びエタノー
ルからそれぞれ1回ずつ再結晶を行なえば、白色
無定形晶状のリゾレシチン2gを得る。(実施例1
と同様に考えると収率は78.8%である。)
Example 1 Only the egg yolk is separated from 100 commercially available chicken eggs and dispersed in 2.5 liters of distilled water. Dissolve 4.4 g of calcium chloride dihydrate in 200 ml of distilled water and 5.0 g of sodium deoxycholate in distilled water.
200 ml of pancreatin (Wako Pure Chemical Industries, Ltd.) and 100 g of pancreatin (manufactured by Wako Pure Chemical Industries, Ltd.) suspended in 200 ml of distilled water were added to the above dispersion and heated to 30-35°C.
Stir for 3 hours. Next, the reaction solution is heated at 105 to 110°C for 3 hours on a water bath in which calcium chloride is dissolved. After cooling, centrifugal dehydration is performed to obtain 1.1 kg of a yellow-brown substance. Add 1.2 methanol to this,
After stirring at room temperature for 30 minutes, filter out insoluble materials. Furthermore, methanol 1.6, 1.6, 1.0 is added to this, the extraction is repeated, and the extracts are collected and concentrated under normal pressure to a volume of 2. Next, 2 parts of chloroform and 1 part of water are added, and the chloroform layer is separated. Furthermore, 400 ml of chloroform is added to the aqueous layer, the chloroform layer is separated, and the obtained chloroform solution is combined and the solvent is distilled off under reduced pressure to obtain 480 g of a brown substance. (This brown substance is referred to as crude product 1.) Next, add 1 part of 80% methanol aqueous solution to this crude product 1.
Add 400ml of n-hexane, separate the lower layer, and add 500ml of 80% methanol aqueous solution to the upper layer solution.
Add and separate the lower layer. The resulting methanol aqueous solution was combined and the solvent was distilled off under reduced pressure. Add 200 ml of ethanol to the residue, filter out the insoluble materials, and distill off the solvent from the filtrate under reduced pressure. Next, add 200 ml of isopropanol and filter out the insoluble materials. If the solvent is distilled off from the filtrate under reduced pressure and then dehydrated by azeotroping with toluene, 133g of pale yellow substance is obtained.
get. This is recrystallized once each from pyridine and ethanol to obtain 29 g of white amorphous crystalline lysolecithin. (In addition, in one chicken egg yolk,
It is said that 500 to 700 mg of lecithin is contained, so if one chicken egg yolk contains 600 ml of lecithin, the yield in this example is 71.4%. ) IR (KBr) cm -1 1720, 1460, 1235, 1080, 1050, 960 NMR (CDC1 8 ) τ value 6.10 (9H) 6.80 (9H) 7.65 (2H) 8.70 (27H) 9.10 (3H) Optical rotation [α ] 20/D = -2.75 (C = 11.5, CHC1 3 :
CH 3 OH = 4:1) [α] 20/D = -0.66 (C = 10.6, CHC1 3 :
CH 3 OH = 1:1) Example 2 To 1480 g of the crude product obtained in Example 1, 800 ml of pyridine was added and dissolved by heating. After standing overnight, filter out the precipitated crystals and add 200 ml of ethanol to it.
ml, filter out the insoluble matter and add ether to the filtrate.
When 500ml is quickly added, 37g of white crystals precipitate out. This is collected and recrystallized once each from pyridine and ethanol to obtain 2 g of lysolecithin in the form of white amorphous crystals. (Example 1
Considering the same way, the yield is 78.8%. )

Claims (1)

【特許請求の範囲】 1 牛脳、豚脳、鶏卵黄または大豆ホモジネート
に、豚すい臓抽出酵素パンクレアチンを作用さ
せ、反応後加熱処理することを特徴とする天然型
リゾレシチン(リゾホスフアチジルコリン)の製
造法。 2 鶏卵黄ホモジネートを用いる特許請求の範囲
第1項記載の天然型リゾレシチンの製造法。 3 豚すい臓抽出酵素パンクレアチンを作用させ
る温度が、15〜50℃である特許請求の範囲第1項
記載の天然型リゾレシチンの製造法。 4 加熱処理を50〜120℃の温度で行う特許請求
の範囲第1項記載の天然型リゾレシチンの製造
法。
[Scope of Claims] 1. A natural lysolecithin (lysophosphatidylcholine) characterized in that cow brain, pig brain, chicken egg yolk or soybean homogenate is reacted with pancreatin, an enzyme extracted from pig pancreas, and heat-treated after the reaction. manufacturing method. 2. The method for producing natural lysolecithin according to claim 1, using chicken egg yolk homogenate. 3. The method for producing natural lysolecithin according to claim 1, wherein the temperature at which the porcine pancreas extract enzyme pancreatin is applied is 15 to 50°C. 4. The method for producing natural lysolecithin according to claim 1, wherein the heat treatment is performed at a temperature of 50 to 120°C.
JP7151778A 1978-06-15 1978-06-15 Novel preparation of natural lysolecithin Granted JPS55315A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7151778A JPS55315A (en) 1978-06-15 1978-06-15 Novel preparation of natural lysolecithin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7151778A JPS55315A (en) 1978-06-15 1978-06-15 Novel preparation of natural lysolecithin

Publications (2)

Publication Number Publication Date
JPS55315A JPS55315A (en) 1980-01-05
JPS6130555B2 true JPS6130555B2 (en) 1986-07-14

Family

ID=13462978

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7151778A Granted JPS55315A (en) 1978-06-15 1978-06-15 Novel preparation of natural lysolecithin

Country Status (1)

Country Link
JP (1) JPS55315A (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60163888A (en) * 1984-02-03 1985-08-26 Pola Chem Ind Inc Production of lipid component
JPH0761274B2 (en) * 1986-08-11 1995-07-05 旭電化工業株式会社 Enzymatic degradation method of phospholipid
JPH0620525B2 (en) * 1986-11-26 1994-03-23 キユーピー株式会社 Method of manufacturing emulsified material
JP2792091B2 (en) * 1989-04-12 1998-08-27 日本油脂株式会社 Method for producing 1-acyl-lysophosphatidylcholine
CN111363771B (en) * 2020-03-18 2023-03-14 湖北瑞邦生物科技有限公司 Production process of pig brain extract with strong oxidation resistance and pig brain extract

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4034124A (en) * 1974-11-25 1977-07-05 Lever Brothers Company Emulsions

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4034124A (en) * 1974-11-25 1977-07-05 Lever Brothers Company Emulsions

Also Published As

Publication number Publication date
JPS55315A (en) 1980-01-05

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