JP2003096095A - Purifying method of protein - Google Patents
Purifying method of proteinInfo
- Publication number
- JP2003096095A JP2003096095A JP2001296433A JP2001296433A JP2003096095A JP 2003096095 A JP2003096095 A JP 2003096095A JP 2001296433 A JP2001296433 A JP 2001296433A JP 2001296433 A JP2001296433 A JP 2001296433A JP 2003096095 A JP2003096095 A JP 2003096095A
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- JP
- Japan
- Prior art keywords
- protein
- buffer solution
- lipid
- water
- soluble polymer
- 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.)
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Links
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- Extraction Or Liquid Replacement (AREA)
- Peptides Or Proteins (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、脂質を含有するヒ
ト血漿由来の蛋白質沈殿画分、特にハプトグロ沈殿画分
ビンから、迅速且つ簡便に脂質を除去する蛋白質の精製
法に関する。TECHNICAL FIELD The present invention relates to a method for purifying a protein which removes lipid from a lipid-containing protein precipitation fraction derived from human plasma, particularly a haptoglo precipitation fraction bottle, rapidly and simply.
【0002】[0002]
【従来の技術】医薬として用いられるヒト血漿由来の蛋
白質には種々のものがあるが、それらは生理活性の分
離、副作用の抑制などの観点からいずれもできる限り精
製されたものであることが望ましい。ハプトグロビンは
分子量8万5千〜40万のヒト血漿由来の蛋白質の一種
であり、遊離しているヘモグロビンと特異的に結合して
複合体を形成し、代謝経路である肝臓に運ばれる。しか
しハプトグロビンの量が遊離のヘモグロビン量よりも少
ないと、遊離ヘモグロビンが血漿中に存在することにな
り、その結果としてヘモグロビン血症やヘモグロビン尿
症などを引き起こす。火傷、輸血、外科手術の際には、
溶血により大量の遊離ヘモグロビンが組織や血中に生成
してくるので、それによって引き起こされるヘモグロビ
ン血症やヘモグロビン尿症の予防、治療のためにハプト
グロビンの投与は有効とされている。ハプトグロビン
は、たとえばヒト血漿のα−およびβ−グロブリン画分
より抽出精製されることが知られている(日本国特許第
958774号)。ところで、当該画分には脂質等の夾
雑物(例えば、リポ蛋白など)が含まれているために、
当該画分の水溶液は混濁している。そこで、その水溶液
を清澄化して、その後の操作を円滑に進めることが必要
となる。この方法としては、ヒト血漿のα−およびβ−
グロブリン画分の水溶液にアクリノールを添加して夾雑
物を沈殿させ、上清を回収した後、アクリノールを除く
ために透析又は吸着処理を行う方法、又はコロイド珪酸
と接触させる方法(特開昭63−17899)が知られ
ている。しかしこれらの方法は、操作が複雑でり、効果
も十分ではなかった。BACKGROUND OF THE INVENTION There are various human plasma-derived proteins used as pharmaceuticals, and it is desirable that they are purified as much as possible from the viewpoints of separation of physiological activity and suppression of side effects. . Haptoglobin is a kind of human plasma-derived protein having a molecular weight of 85,000 to 400,000, and specifically binds to free hemoglobin to form a complex, which is transported to the liver which is a metabolic pathway. However, when the amount of haptoglobin is less than the amount of free hemoglobin, free hemoglobin is present in plasma, resulting in hemoglobinemia and hemoglobinuria. In case of burns, blood transfusions, surgery
Since a large amount of free hemoglobin is produced in tissues and blood by hemolysis, administration of haptoglobin is considered effective for the prevention and treatment of hemoglobinemia and hemoglobinuria caused thereby. Haptoglobin is known to be extracted and purified from, for example, the α- and β-globulin fractions of human plasma (Japanese Patent No. 957774). By the way, since the fraction contains impurities such as lipids (for example, lipoprotein),
The aqueous solution of the fraction is cloudy. Therefore, it is necessary to clarify the aqueous solution so that the subsequent operation can proceed smoothly. As this method, human plasma α- and β-
After adding acrinol to the aqueous solution of the globulin fraction to precipitate impurities and collecting the supernatant, a method of performing dialysis or adsorption treatment for removing acrinol, or a method of contacting with colloidal silicic acid (JP-A-63- 17899) is known. However, these methods are complicated in operation and not sufficiently effective.
【0003】[0003]
【発明が解決しようとする課題】このような状況のもと
に、本発明は、脂質を含むヒト血漿由来の蛋白質溶液か
ら簡便且つ迅速に脂質を分離、除去して、脂質含量が低
減された蛋白質、特にハプトグロビンを迅速且つ簡便に
取得することを目的としている。Under these circumstances, the present invention has achieved a simple and rapid lipid separation and removal from a lipid-containing protein solution derived from human plasma, thereby reducing the lipid content. The purpose is to obtain proteins, especially haptoglobin, quickly and conveniently.
【0004】[0004]
【課題を解決するための手段】本発明者らは、上記課題
を解決するため種々研究を重ねた結果、原料として例え
ば、コーンの低温エタノール分画法による第IV、IV−1
またはIV−4画分を、水溶性ポリマーを含む緩衝液と接
触させると、脂質は溶解せず蛋白質は溶解してくるの
で、その上清から蛋白質、特にハプトグロビンを採取す
るという方法によって、容易且つ迅速に脂質含量の低減
された蛋白質画分が得られることを知見し、その知見に
基づいてさらに研究を重ねて本発明を完成した。The inventors of the present invention have conducted various studies to solve the above-mentioned problems, and as a result, as a raw material, for example, corn IV-IV-1 by the low temperature ethanol fractionation method was used.
Alternatively, when the IV-4 fraction is brought into contact with a buffer solution containing a water-soluble polymer, the lipid is not dissolved and the protein is dissolved, so that the protein, particularly haptoglobin, can be collected from the supernatant easily and easily. It was found that a protein fraction with a reduced lipid content can be rapidly obtained, and further studies were conducted based on the findings to complete the present invention.
【0005】すなわち、本発明は、(1)ヒト血漿由来
の脂質を含有する蛋白質画分を水溶性ポリマーを含む緩
衝液と接触させ、その上清から蛋白質を採取することを
特徴とする蛋白質の精製法、(2)蛋白質画分がコーン
の低温エタノール分画法による第IV、IV−1またはIV−
4画分であり、蛋白質がハプトグロビンである(1)又
は(2)記載の精製法、(3)水溶性ポリマーが分子量
400〜10000のポリオキシエチレングリコールで
ある(1)又は(2)記載の精製法、(4)緩衝液がリ
ン酸緩衝液、酢酸緩衝液およびクエン酸緩衝液から選ば
れた少なくとも1種である(1)又は(2)記載の精製
法、および(5)水溶性ポリマーを含む緩衝液が、水溶
性ポリマーを0.5〜10.0w/v%含む0.1〜3
00mM濃度の緩衝液である(1)又は(2)記載の精
製法、である。That is, according to the present invention, (1) a protein fraction containing a lipid derived from human plasma is brought into contact with a buffer solution containing a water-soluble polymer, and the protein is collected from the supernatant thereof. Purification method (2) IV-IV-1 or IV- by the low temperature ethanol fractionation method in which the protein fraction is corn
4 fractions, wherein the protein is haptoglobin, the purification method according to (1) or (2), (3) The water-soluble polymer is polyoxyethylene glycol having a molecular weight of 400 to 10,000, according to (1) or (2) Purification method, (4) The purification method according to (1) or (2), wherein the buffer solution is at least one selected from a phosphate buffer solution, an acetate buffer solution, and a citrate buffer solution, and (5) a water-soluble polymer. The buffer solution containing 0.5 to 10.0 w / v% of the water-soluble polymer is 0.1 to 3
The purification method according to (1) or (2), which is a buffer solution having a concentration of 00 mM.
【0006】[0006]
【発明の実施の形態】本発明の原料として用いられるヒ
ト血漿由来の蛋白質画分は、α−およびβ−グロブリン
画分、コーン低温エタノール分画法の第IV、IV-1、IV
−4等の各沈殿画分から調製することができる。これら
の蛋白質沈殿画分は、通常コレステロール、リン脂質脂
質等の脂質を比較的豊富に含んでいることが多い。BEST MODE FOR CARRYING OUT THE INVENTION The human plasma-derived protein fractions used as the raw material of the present invention include α- and β-globulin fractions, IV-IV-1 and IV-IV of the corn low temperature ethanol fractionation method.
It can be prepared from each precipitation fraction such as -4. These protein-precipitated fractions usually contain relatively abundant lipids such as cholesterol and phospholipid lipids in many cases.
【0007】本発明では脂質を含む原料蛋白質を先ず水
溶性ポリマーを含む緩衝液と接触させる。この操作によ
り、蛋白質は緩衝液中に溶解し、脂質は液中に不溶物と
して残存してくる。水溶性ポリマーは、分子中に水酸基
等の親水性基を有し、水と混じり合う性質を有するポリ
マーであり、ポリエチレングリコール(分子量400〜
10,000)、デキストラン、メチルセルロース、ポ
リビニルピロリドン、ポリビニルアルコールなどが例と
して挙げられるが、好ましいものは分子量1000〜6
000のポリエチレングリコールである。緩衝液はリン
酸緩衝液、酢酸緩衝液、クエン酸緩衝液などが挙げられ
るが、リン酸緩衝液やリン酸−NaCl緩衝液が好まし
い。緩衝液のpHは、通常4.5〜7.0、好ましくは
4.8〜6.0である。また混合液中の緩衝液の濃度
は、0.1〜300mM、好ましくは、1〜100m
M、さらに好ましくは5〜50mMであるIn the present invention, a raw material protein containing a lipid is first contacted with a buffer solution containing a water-soluble polymer. By this operation, the protein is dissolved in the buffer solution and the lipid remains in the solution as an insoluble matter. The water-soluble polymer is a polymer having a hydrophilic group such as a hydroxyl group in the molecule and having a property of being mixed with water, and polyethylene glycol (having a molecular weight of 400 to
10,000), dextran, methyl cellulose, polyvinylpyrrolidone, polyvinyl alcohol and the like are mentioned as examples, but a preferable one is a molecular weight of 1000-6.
000 polyethylene glycol. Examples of the buffer solution include a phosphate buffer solution, an acetate buffer solution, a citrate buffer solution, and the like, and a phosphate buffer solution and a phosphate-NaCl buffer solution are preferable. The pH of the buffer solution is usually 4.5 to 7.0, preferably 4.8 to 6.0. The concentration of the buffer solution in the mixed solution is 0.1 to 300 mM, preferably 1 to 100 m.
M, more preferably 5 to 50 mM
【0008】水溶性ポリマーを含む緩衝液中の水溶性ポ
リマーの濃度は、通常0.5〜10%(w/v)、好ま
しくは2〜6%(w/v)である。。接触は、1分〜2
時間、好ましくは10分〜1時間行う。接触時の温度
は、常温又は冷却下に行うのがよい。接触は、回分式で
もよく、また連続式でもよい。このようにして得られた
液から脂質を含む不溶物を除去する。不溶物の除去は、
どのような方法でもよいが、通常フィルターによる濾過
又は遠心分離が好ましい。The concentration of the water-soluble polymer in the buffer containing the water-soluble polymer is usually 0.5 to 10% (w / v), preferably 2 to 6% (w / v). . Contact from 1 minute to 2
The time is preferably 10 minutes to 1 hour. The contact temperature is preferably room temperature or under cooling. The contact may be a batch type or a continuous type. Insoluble matter containing lipids is removed from the liquid thus obtained. Insoluble matter can be removed by
Although any method may be used, filtration with a filter or centrifugation is usually preferable.
【0009】濾液に、例えば、硫酸アンモニウムを加
え、沈殿物を採取する。沈殿物を水に溶解し、いわゆる
ウイルス不活化のための加熱処理(通常50〜70℃、
1〜24時間)を行う。加熱処理した液を、必要により
陰イオン交換クロマトグラフィーにかけて精製する。得
られた蛋白質溶液、とくにハプトグロビン溶液は、さら
に公知の製剤化技術を組み合わせることにより、臨床上
適応できる蛋白製剤、特にハプトグロビン製剤とするこ
とができる。例えば、安定化剤、賦形剤等の添加、小分
け分注、透析、限外濾過、凍結乾燥等を施すことができ
る。Ammonium sulfate, for example, is added to the filtrate to collect the precipitate. The precipitate is dissolved in water, and heat treatment for so-called virus inactivation (usually 50 to 70 ° C,
1 to 24 hours). If necessary, the heat-treated liquid is purified by subjecting it to anion exchange chromatography. The obtained protein solution, especially haptoglobin solution, can be made into a clinically applicable protein preparation, especially haptoglobin preparation, by further combining known formulation techniques. For example, stabilizers, excipients, etc. can be added, subdivision, dialysis, ultrafiltration, lyophilization, etc. can be performed.
【0010】[0010]
【実施例】以下に実施例、比較例および実験例を挙げて
本発明をより具体的に説明する。
実施例1
ヒト血漿由来のコーン低温エタノール分画法で分画した
IV−4沈殿画分各14gに、PEG4000を0〜10
w/v%含む20mMリン酸−10mMNaCl緩衝液
(pH4.9)15ミリリットルを加えて、室温下約1
5分攪拌し、フィルターで濾過して濾液を採取した。EXAMPLES The present invention will be described more specifically with reference to Examples, Comparative Examples and Experimental Examples. Example 1 Fractionation by the Cohn low temperature ethanol fractionation method derived from human plasma
PEG4000 was added to each of the IV-4 precipitate fractions of 14 g in an amount of 0 to 10
Add 15 ml of 20 mM phosphoric acid-10 mM NaCl buffer (pH 4.9) containing w / v%, and add about 1 at room temperature.
The mixture was stirred for 5 minutes, filtered through a filter, and the filtrate was collected.
【0011】比較例1
PEG4000を含まない20mMリン酸−10mMN
aCl緩衝液(pH4.9)を用いて実施例1と同様の
方法で抽出操作を行った。
試験例1
実施例1および比較例1で得られた濾液中の総リン脂
質、コレステロールの量および蛋白(ハプトグロビン)
量を測定し、〔表1〕に示す結果を得た。Comparative Example 1 20 mM phosphoric acid-10 mMN without PEG4000
Extraction operation was performed in the same manner as in Example 1 using an aCl buffer (pH 4.9). Test Example 1 Total phospholipids, cholesterol amount and protein (haptoglobin) in the filtrates obtained in Example 1 and Comparative Example 1
The amount was measured and the results shown in [Table 1] were obtained.
【0012】[0012]
【表1】
上記〔表1〕から明らかなように、リン酸−NaCl緩
衝液単独使用に比して、PEG4000を併用した場合
は、脂質含量が大幅に低減された。[Table 1] As is clear from the above [Table 1], the lipid content was significantly reduced when PEG4000 was used in combination as compared with the case where the phosphate-NaCl buffer solution was used alone.
【0013】[0013]
【発明の効果】本発明は、ヒト血漿由来の蛋白質画分、
特にコーン低温エタノール分画法による第IV画分等を、
水溶性ポリマーを含む緩衝液で処理(抽出)するだけ
で、簡便且つ迅速に脂質含量の低減された蛋白質溶液を
得ることができる。The present invention provides a protein fraction derived from human plasma,
Especially, the IV fraction etc. by the corn low temperature ethanol fractionation method,
A protein solution having a reduced lipid content can be simply and rapidly obtained by simply treating (extracting) with a buffer solution containing a water-soluble polymer.
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D056 AB17 AC20 CA01 CA05 CA14 DA10 4H045 AA20 BA55 CA42 GA05 ─────────────────────────────────────────────────── ─── Continued front page F-term (reference) 4D056 AB17 AC20 CA01 CA05 CA14 DA10 4H045 AA20 BA55 CA42 GA05
Claims (5)
を水溶性ポリマーを含む緩衝液と接触させ、その上清か
ら蛋白質を採取することを特徴とする蛋白質の精製法。1. A method for purifying a protein, which comprises contacting a protein fraction containing a lipid derived from human plasma with a buffer containing a water-soluble polymer, and collecting the protein from the supernatant.
法による第IV、IV−1またはIV−4画分であり、蛋白質
がハプトグロビンである請求項1記載の精製法。2. The purification method according to claim 1, wherein the protein fraction is the IV, IV-1 or IV-4 fraction obtained by Cohn's low temperature ethanol fractionation method, and the protein is haptoglobin.
00のポリオキシエチレングリコールである請求項1又
は2記載の精製法。3. The water-soluble polymer has a molecular weight of 400 to 100.
The method according to claim 1 or 2, wherein the polyoxyethylene glycol is 00.
クエン酸緩衝液から選ばれた少なくとも1種である請求
項1又は2記載の精製法。4. The purification method according to claim 1 or 2, wherein the buffer solution is at least one selected from a phosphate buffer solution, an acetate buffer solution and a citrate buffer solution.
リマーを0.5〜10.0w/v%含む0.1〜300
mM濃度の緩衝液である請求項1又は2記載の精製法。5. A buffer solution containing a water-soluble polymer in an amount of 0.1 to 300 containing 0.5 to 10.0 w / v% of the water-soluble polymer.
The purification method according to claim 1 or 2, which is a buffer solution having a mM concentration.
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JP2001296433A JP4703922B2 (en) | 2001-09-27 | 2001-09-27 | Protein purification method |
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Family
ID=19117679
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9534029B2 (en) | 2012-10-03 | 2017-01-03 | Csl Behring Ag | Method of purifying proteins |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5077516A (en) * | 1973-11-15 | 1975-06-24 | ||
JPH03128398A (en) * | 1989-07-12 | 1991-05-31 | Green Cross Corp:The | Method for fractionating blood plasma protein |
JPH0892287A (en) * | 1994-09-28 | 1996-04-09 | Green Cross Corp:The | Production of haptoglobin |
JPH1081699A (en) * | 1996-07-15 | 1998-03-31 | Green Cross Corp:The | Removal of discoloration substance |
-
2001
- 2001-09-27 JP JP2001296433A patent/JP4703922B2/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5077516A (en) * | 1973-11-15 | 1975-06-24 | ||
JPH03128398A (en) * | 1989-07-12 | 1991-05-31 | Green Cross Corp:The | Method for fractionating blood plasma protein |
JPH0892287A (en) * | 1994-09-28 | 1996-04-09 | Green Cross Corp:The | Production of haptoglobin |
JPH1081699A (en) * | 1996-07-15 | 1998-03-31 | Green Cross Corp:The | Removal of discoloration substance |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9534029B2 (en) | 2012-10-03 | 2017-01-03 | Csl Behring Ag | Method of purifying proteins |
US9937229B2 (en) | 2012-10-03 | 2018-04-10 | Csl Behring Ag | Methods of treatment using hemopexin compositions |
US10918696B2 (en) | 2012-10-03 | 2021-02-16 | Csl Behring Ag | Methods of treatment using hemopexin compositions |
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Free format text: JAPANESE INTERMEDIATE CODE: R250 |
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LAPS | Cancellation because of no payment of annual fees |