JPH03284693A - Carrier for gel-filtration - Google Patents
Carrier for gel-filtrationInfo
- Publication number
- JPH03284693A JPH03284693A JP2082924A JP8292490A JPH03284693A JP H03284693 A JPH03284693 A JP H03284693A JP 2082924 A JP2082924 A JP 2082924A JP 8292490 A JP8292490 A JP 8292490A JP H03284693 A JPH03284693 A JP H03284693A
- Authority
- JP
- Japan
- Prior art keywords
- gel
- carrier
- separation
- proteins
- cellulose
- 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.)
- Pending
Links
- 238000002523 gelfiltration Methods 0.000 title claims description 15
- 229920002230 Pectic acid Polymers 0.000 claims abstract description 22
- 239000000126 substance Substances 0.000 claims abstract description 14
- LCLHHZYHLXDRQG-ZNKJPWOQSA-N pectic acid Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)O[C@H](C(O)=O)[C@@H]1OC1[C@H](O)[C@@H](O)[C@@H](OC2[C@@H]([C@@H](O)[C@@H](O)[C@H](O2)C(O)=O)O)[C@@H](C(O)=O)O1 LCLHHZYHLXDRQG-ZNKJPWOQSA-N 0.000 claims abstract description 6
- 239000010318 polygalacturonic acid Substances 0.000 claims abstract description 6
- PTHCMJGKKRQCBF-UHFFFAOYSA-N Cellulose, microcrystalline Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC)C(CO)O1 PTHCMJGKKRQCBF-UHFFFAOYSA-N 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 15
- 229920003169 water-soluble polymer Polymers 0.000 claims description 5
- 102000004169 proteins and genes Human genes 0.000 abstract description 25
- 108090000623 proteins and genes Proteins 0.000 abstract description 25
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract description 12
- 238000000926 separation method Methods 0.000 abstract description 10
- 239000011780 sodium chloride Substances 0.000 abstract description 6
- 241000196324 Embryophyta Species 0.000 abstract description 5
- 239000003431 cross linking reagent Substances 0.000 abstract description 5
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 abstract description 4
- 150000002576 ketones Chemical class 0.000 abstract description 4
- 229920001277 pectin Polymers 0.000 abstract description 4
- 239000001814 pectin Substances 0.000 abstract description 4
- 235000010987 pectin Nutrition 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 4
- 235000020971 citrus fruits Nutrition 0.000 abstract description 3
- 238000004132 cross linking Methods 0.000 abstract description 3
- 239000000843 powder Substances 0.000 abstract description 3
- 239000002253 acid Substances 0.000 abstract description 2
- 150000001408 amides Chemical class 0.000 abstract description 2
- 150000002148 esters Chemical class 0.000 abstract description 2
- 239000002245 particle Substances 0.000 abstract description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 1
- 230000000903 blocking effect Effects 0.000 abstract 1
- 239000002198 insoluble material Substances 0.000 abstract 1
- 239000000499 gel Substances 0.000 description 33
- AEMOLEFTQBMNLQ-BKBMJHBISA-N alpha-D-galacturonic acid Chemical compound O[C@H]1O[C@H](C(O)=O)[C@H](O)[C@H](O)[C@H]1O AEMOLEFTQBMNLQ-BKBMJHBISA-N 0.000 description 17
- 229920002678 cellulose Polymers 0.000 description 17
- 235000010980 cellulose Nutrition 0.000 description 17
- 239000001913 cellulose Substances 0.000 description 16
- 230000000694 effects Effects 0.000 description 15
- 239000000969 carrier Substances 0.000 description 8
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- 150000004676 glycans Chemical class 0.000 description 6
- 229920001282 polysaccharide Polymers 0.000 description 6
- 239000005017 polysaccharide Substances 0.000 description 6
- 238000000746 purification Methods 0.000 description 6
- 238000004587 chromatography analysis Methods 0.000 description 5
- 239000003480 eluent Substances 0.000 description 5
- 102000004190 Enzymes Human genes 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 3
- 238000001742 protein purification Methods 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229920001059 synthetic polymer Polymers 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 229920005654 Sephadex Polymers 0.000 description 2
- 239000008351 acetate buffer Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000000872 buffer Substances 0.000 description 2
- 238000005227 gel permeation chromatography Methods 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 238000004255 ion exchange chromatography Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229930014626 natural product Natural products 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 229920000936 Agarose Polymers 0.000 description 1
- 241001474374 Blennius Species 0.000 description 1
- 102000016938 Catalase Human genes 0.000 description 1
- 108010053835 Catalase Proteins 0.000 description 1
- 241000207199 Citrus Species 0.000 description 1
- 241000555678 Citrus unshiu Species 0.000 description 1
- 229920002307 Dextran Polymers 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- 102000001390 Fructose-Bisphosphate Aldolase Human genes 0.000 description 1
- 108010068561 Fructose-Bisphosphate Aldolase Proteins 0.000 description 1
- 108010059820 Polygalacturonase Proteins 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 239000012507 Sephadex™ Substances 0.000 description 1
- 238000000944 Soxhlet extraction Methods 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 239000011543 agarose gel Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 230000009435 amidation Effects 0.000 description 1
- 238000007112 amidation reaction Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 238000011033 desalting Methods 0.000 description 1
- -1 dextran gel Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000011067 equilibration Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 229920001002 functional polymer Polymers 0.000 description 1
- 238000001641 gel filtration chromatography Methods 0.000 description 1
- 102000034238 globular proteins Human genes 0.000 description 1
- 108091005896 globular proteins Proteins 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000008057 potassium phosphate buffer Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000002000 scavenging effect Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 230000002522 swelling effect Effects 0.000 description 1
- 239000013076 target substance Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Treatment Of Liquids With Adsorbents In General (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Peptides Or Proteins (AREA)
- Enzymes And Modification Thereof (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はペクチン酸セルロースゲルからなるゲル濾過用
担体、特に濾過用担体及び該担体を用いて水溶性高分子
物質、特に蛋白質を精製する方法に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a carrier for gel filtration made of cellulose pectate gel, particularly a carrier for filtration, and a method for purifying water-soluble polymeric substances, especially proteins, using the carrier. It is related to.
水溶性高分子物質、特に蛋白質の分離、精製は各種生化
学的研究などの分野で広く行われている。Background of the Invention Separation and purification of water-soluble polymeric substances, especially proteins, is widely carried out in various biochemical research fields.
分離、精製された蛋白質を得ることは、該蛋白質の性質
を研究するために重要であり、かつ分離、精製された蛋
白質を各種の生化学反応に応用することもまた重要なこ
ととなっている。また近年、機能性高分子としての蛋白
質、酵素の工業的需要が食品、製薬、化学等の諸分野に
おいてますます高まりつつある。Obtaining isolated and purified proteins is important for studying the properties of the proteins, and it is also important to apply the isolated and purified proteins to various biochemical reactions. . In addition, in recent years, industrial demand for proteins and enzymes as functional polymers has been increasing more and more in various fields such as food, pharmaceuticals, and chemistry.
従来、蛋白質の分離、精製法としてクロマトグラフィー
法の果す役割は非常に大きなものであり、中でも、ゲル
濾過(ゲルクロマトグラフィー)法は最も繁用されてい
る手法の一つである。該方法は、球状蛋白質の分子量差
にのみ基く分子篩効果による分離モードであり、イオン
的性質や疎水的性質等による影響を排除した条件下で行
われる為、殆どの蛋白質、酵素に同時に適応できる点で
非常に汎用性が高くかつ鋭敏な分離手法である。Conventionally, chromatography has played a very important role as a protein separation and purification method, and gel filtration (gel chromatography) is one of the most frequently used methods. This method is a separation mode based on the molecular sieve effect based only on the molecular weight difference of globular proteins, and is carried out under conditions that exclude the effects of ionic and hydrophobic properties, so it can be applied to most proteins and enzymes simultaneously. This is a very versatile and sensitive separation method.
該方法に使用されるゲルクロマト用担体は合成ポリマー
系、天然多糖系の2種類に大別することができるが、い
ずれの担体についても一長一短があり、それがゲル濾過
法による蛋白質精製の、ともすれば敬遠されがちな、技
術的難易度の高さともなっており、工業的利用が一部の
高付加価値品のみに限られている理由と考えられる。即
ち、例えば合成ポリマー系担体としては、ポリビニルア
ルコール、ポリアクリルアミド樹脂等の水溶性ポリマー
を架橋により不溶化ゲルとしたものが代表とされるが、
いずれの樹脂も強度的には天然多糖由来の担体と比べて
も高い特性を保持しているが、本来、非天然物であるこ
とより、蛋白質との親和性が低いことや、疎水的吸着等
の非特異的吸着による変性、失活等の収率低下が起こり
易い為、クロマトカラムからの蛋白質の安定的な回収に
問題があった。The carriers for gel chromatography used in this method can be roughly divided into two types: synthetic polymer-based and natural polysaccharide-based, but each carrier has its advantages and disadvantages, and these are important for protein purification by gel filtration. Therefore, it is often avoided due to its high degree of technical difficulty, which is thought to be the reason why its industrial use is limited to only a few high value-added products. That is, for example, synthetic polymer carriers are typically made into insolubilized gels by crosslinking water-soluble polymers such as polyvinyl alcohol and polyacrylamide resins.
Both resins have strong properties compared to carriers derived from natural polysaccharides, but since they are non-natural products, they have low affinity with proteins, hydrophobic adsorption, etc. Since yield reductions such as denaturation and deactivation due to non-specific adsorption of proteins tend to occur, there has been a problem in stable recovery of proteins from chromatography columns.
また、天然多糖系担体としては、デキストランゲル等の
微生物多糖や、アガロースゲル等の海藻系及びセルロー
ス類か若しくはそれらを架橋処理したものが最も一般的
に用いられている。これらの担体に共通する特徴的なこ
ととしては合成ポリマー系に比べ、担体自体の天然物か
らの抽出、精製、ゲルの調製にコストがかかり、全体的
に高価であることである。また、デキストラン系及びア
ガロース系担体は蛋白質精製用に調製したものは、膨潤
率が高く柔弱な為、ゲル濾過カラム中乙こおいて溶離液
を高速で流すことができない。セルロース系担体は一般
に他の天然多糖に比べ比較的安価で強度も高いというメ
リットを持っているが、その高い結晶構造の為、巨大網
目状構造をとるゲル濾過用担体に比して、高分子量物の
分画にはあまり通さない。このような理由からゲル濾過
法が優れた分離、精製手法であるにも拘わらず工業的な
利用が制限されているのが現状である。Furthermore, as natural polysaccharide carriers, microbial polysaccharides such as dextran gel, seaweeds such as agarose gel, celluloses, or crosslinked products thereof are most commonly used. A common characteristic of these carriers is that, compared to synthetic polymer systems, extraction from natural products of the carrier itself, purification, and gel preparation are costly, making them expensive overall. In addition, dextran and agarose carriers prepared for protein purification have a high swelling rate and are weak, making it impossible to flow the eluent at high speed through the gel filtration column. Cellulose-based carriers generally have the advantage of being relatively cheap and strong compared to other natural polysaccharides, but due to their highly crystalline structure, they have a higher molecular weight than gel filtration carriers that have a large network structure. It does not pass through the fractionation of substances very well. For these reasons, although gel filtration is an excellent separation and purification method, its industrial use is currently limited.
発明者等は、かかる現状に鑑み、より安価で物理的、化
学的強度に優れ、かつ蛋白質等の不安定な化合物に対し
てもより高い親和性をもった新しいゲル濾過用の素材の
検索を鋭意行った結果、ペクチン酸セルロースゲルが、
分子篩特性、蛋白との親和性及び物理的化学的強度にお
いて非常に優れた特性を有することを見い出し、本発明
を完成するに至った。In view of the current situation, the inventors searched for a new material for gel filtration that is cheaper, has excellent physical and chemical strength, and has a higher affinity for unstable compounds such as proteins. As a result of diligent research, cellulose pectate gel was
It was discovered that it has very excellent properties in terms of molecular sieve properties, affinity with proteins, and physical and chemical strength, leading to the completion of the present invention.
即ち、本発明の第一の特徴はゲル濾過用担体としてのペ
クチン酸セルロースゲルの利用であり、第二の特徴は、
該ゲルを用いて水溶性高分子¥!A′Jt、特に蛋白質
を分離、精製する方法にある。That is, the first feature of the present invention is the use of pectic acid cellulose gel as a carrier for gel filtration, and the second feature is:
Use this gel to create water-soluble polymers! A'Jt, especially a method for separating and purifying proteins.
本発明で用いられるペクチン酸セルロースゲルはペクチ
ン含有植物から調製されるものであり、その製造法とし
ては、例えば本発明者等が先に出願した(特願平1−2
96199号)方法が好適である。The cellulose pectate gel used in the present invention is prepared from pectin-containing plants, and the method for its production is, for example, disclosed in the patent application filed by the present inventors previously (Japanese Patent Application No.
No. 96199) method is preferred.
この方法は、例えば柑橘類果皮等のペクチン含有植物組
織の乾燥粉末をケトン類により半連続抽出して得た抽出
不溶物をケトン類の存在下アルカリ条件下でケン化し、
次いで低級アルコール類マたはケトン類に懸濁後、架橋
試薬により架橋するものである。In this method, for example, dry powder of pectin-containing plant tissue such as citrus peel is semi-continuously extracted with ketones, and the extracted insoluble matter is saponified under alkaline conditions in the presence of ketones.
Next, it is suspended in lower alcohols or ketones, and then crosslinked with a crosslinking reagent.
しかしながら他の製法によって得られるペクチン酸セル
ロースゲルも使用可能であり、本発明において使用する
ペクチン酸セルロースゲルはその製法により特に限定さ
れない。However, cellulose pectate gel obtained by other manufacturing methods can also be used, and the cellulose pectate gel used in the present invention is not particularly limited by its manufacturing method.
L記製法により得られる該ゲルは、ペクチン酸を多(含
有しており、ペクチン酸中のα−D−ガラクチュロン酸
残基に由来するカルボキシル基の効果で、高い重金属補
足能を保持しており水処理用樹脂として有用であること
は公知である(特開昭64−43501号)、また、ペ
クチン酸セルロースゲルは、イオン交換クロマトグラフ
ィー用担体としても非常に高収率で分離、回収でき、こ
れを用いた蛋白質の分離、精製法については既に発明者
等により出願されている (特願平1−296200号
)。The gel obtained by the production method described in L contains a large amount of pectic acid, and has a high heavy metal scavenging ability due to the effect of carboxyl groups derived from α-D-galacturonic acid residues in pectic acid. It is known that cellulose pectate gel is useful as a water treatment resin (Japanese Unexamined Patent Publication No. 64-43501). Cellulose pectate gel can also be used as a carrier for ion exchange chromatography and can be separated and recovered in very high yields. The inventors have already filed an application for a protein separation and purification method using this method (Japanese Patent Application No. 1-296200).
以上の様なペクチン酸セルロースゲルの効果は、該ゲル
が原料植物の細胞壁成分の立体構造を天然状態のまま保
持していることに起因すると考えられる。Hμち、生体
中の能動的、受動的物質輸送の場を保有していることで
、蛋白質等のデリケートな生体物質も安定な状態で移動
できるものと思われる。The effects of cellulose pectate gel as described above are thought to be due to the fact that the gel retains the three-dimensional structure of the cell wall components of the raw material plant in its natural state. Hμ, it is thought that delicate biological substances such as proteins can be transported in a stable state by having a field for active and passive substance transport in living organisms.
この特性はそのままゲル濾過用担体として用いる際にも
有効に働くことが分かった。即ち、イオン交換的効果を
抑える意味で塩化ナトリウム等の対イオンを添加した溶
離液中でクロマトグラフィーを行うか、或いは、エステ
ル、アミド等の共有結合によりウロン酸に由来するカル
ボキシル基をブロックすることによりイオン的相互作用
等の殆ど無い分子篩を得ることが可能である。It was found that this property works effectively when used directly as a carrier for gel filtration. In other words, chromatography is performed in an eluent to which counterions such as sodium chloride are added to suppress ion exchange effects, or carboxyl groups derived from uronic acid are blocked by covalent bonds such as esters and amides. It is possible to obtain a molecular sieve with almost no ionic interactions.
次に、実際にカラムを用いて蛋白質のゲル濾過クロマト
グラフィーを行う場合について説明する。Next, a case in which gel filtration chromatography of proteins is actually performed using a column will be explained.
使用するペクチン酸セルロースゲルのグレードとしては
、1〜10 (モル/!R1残基)、好ましくは2〜5
(モル/糖残基)の架橋剤を用いたゲルが蛋白の分離
には適している。粒径は100〜500μm(乾燥状態
)、出来れば200〜300μ■に揃えることが望まし
い0本ゲルは大きいポアサイズを保持しているものの、
かなり硬質であり、膨潤性が低い為、膨潤に際しては室
温、溶離液中で1時間以内の浸漬で充分である。また、
オートクレーブ(121°C115分)によっても可能
である。本ゲルのクロマトカラムへの充填法、洗浄法、
及び試料の添加法については従来の市販硬質ゲル濾過剤
と同様の処理でよい。The grade of the cellulose pectate gel used is 1 to 10 (mol/!R1 residue), preferably 2 to 5
(mol/sugar residue) gel using a crosslinking agent is suitable for protein separation. The particle size is preferably 100 to 500 μm (dry state), preferably 200 to 300 μm.Although the zero gel maintains a large pore size,
Since it is quite hard and has low swelling properties, it is sufficient to immerse it in an eluent at room temperature for one hour or less for swelling. Also,
It is also possible by autoclaving (121°C for 115 minutes). How to fill this gel into a chromatography column, how to wash it,
The method for adding the sample may be the same as for conventional commercially available hard gel filtration agents.
溶離液については、pH3〜10の本ゲルが安定な領域
の緩衝液が使用でき、クロマトを行う際は目的物質の安
定pH領域で行うことが好ましい。先に述べたようなエ
ステル化、アミド化等の化学的処理によるカルボキシル
基のブロッキングがなされていない該ゲルを用いる場合
は、溶離液中に0.1M〜1.叶のNaC1を添加する
ことが好ましい。As for the eluent, a buffer with a pH of 3 to 10 in which the present gel is stable can be used, and chromatography is preferably performed in a stable pH range of the target substance. When using the gel whose carboxyl groups have not been blocked by chemical treatments such as esterification and amidation as described above, the eluent contains 0.1M to 1.0M. Preferably, leaf NaCl is added.
次に、流速については、本ゲルは硬質ゲルであり、体積
変化が少ない為、例えば、2.5 X 30C111カ
ラムを用いた場合、最大SV5/hr (150ae・
cm−’−hr)の高流速が可能であり、必要に応じて
ポンプにより圧送してもよい(最大操作圧300cm
H,0以上)。Next, regarding the flow rate, since this gel is a hard gel and has little volume change, for example, when using a 2.5 x 30C111 column, the maximum SV5/hr (150ae・
high flow rates (cm-'-hr) are possible, and may be pumped if necessary (maximum operating pressure 300 cm).
H, 0 or more).
カラムからの溶出液は逐次フラクションコレクター等に
より一定量ずつ分取される。The eluate from the column is sequentially collected in fixed amounts using a fraction collector or the like.
以上の操作により分取された目的画分は通常の処理によ
り脱塩、濃縮され、必要に応じて各種クロマト操作を繰
り返した後、電気泳動的均−或いは結晶化されることで
、精製を完了する。The target fraction collected through the above operations is desalted and concentrated through normal processing, and after repeating various chromatographic operations as necessary, is electrophoretically homogenized or crystallized to complete purification. do.
[発明の効果〕
以上説明したごとく、本発明においてペクチン酸セルロ
ースゲルが、水溶性高分子物質、特に蛋白質のゲル濾過
用担体として好適であることが示された。本ゲルは蛋白
質、酵素に対し不活性であり、しかも本ゲル中では安定
な状態での物質移動が可能であるため、カラムよりほぼ
100%近い収率での回収が可能である。また、本ゲル
は堅牢なマトリンクス構造を持ち、天然多糖系ゲルとし
ては非常に高強度であるため高流速で流すことができ、
高速液体クロマトグラフィー用としても使用可能である
。また、ポアサイズを調整することにより、ウィルス等
の巨大分子の分画も可能である。[Effects of the Invention] As explained above, the present invention shows that cellulose pectate gel is suitable as a carrier for gel filtration of water-soluble polymer substances, especially proteins. This gel is inert to proteins and enzymes, and moreover, substances can be transferred in a stable state within this gel, so it is possible to recover at a yield close to 100% compared to a column. In addition, this gel has a robust matrix structure and is extremely strong for a natural polysaccharide gel, so it can be flowed at high flow rates.
It can also be used for high performance liquid chromatography. Furthermore, by adjusting the pore size, it is also possible to fractionate macromolecules such as viruses.
本ゲルは発明者等が特願平1−296199号において
示した様に、柑橘類等のペクチン含有植物のMi織を原
料としており、コスト面での大きなメリントを持つ。こ
れらの結果より、ペクチン酸セルロースゲルは研究室用
としてだけでなく、工業的規模の水溶性高分子物質、特
に蛋白精製にも有用な担体であることが明らかになった
。As the inventors have shown in Japanese Patent Application No. 1-296199, this gel is made from Mi fibers of pectin-containing plants such as citrus fruits, and has a large cost advantage. These results revealed that cellulose pectate gel is a useful carrier not only for laboratory use but also for industrial-scale water-soluble polymeric substances, especially protein purification.
以下に本発明を実施例をもって更に詳しく説明する。尚
本発明はこれらの実施例に限定されるものではない。The present invention will be explained in more detail below with reference to Examples. Note that the present invention is not limited to these examples.
(参考例)
架橋剤2.6モル/糖残基のゲル濾過用ペクチン酸セル
ロースゲルの調製法について述べる。(Reference Example) A method for preparing a cellulose pectate gel for gel filtration containing 2.6 mol of crosslinking agent/sugar residue will be described.
温州みかん果皮の乾燥粉末41gを、60゛Cに加温し
た45重量%アセトン水溶液240紙を用いてソックス
レー抽出を約6時間行い、残ったアセトン不溶物28g
(混晶)を濾取した。これを50重量%アセトン水溶液
とエピクロルヒドリンとの5:l(容積比)の混合液3
50dに加え、攪拌下40°Cに保った。次に、5M
NaOH50dをこれに加え、40″Cで2時間架橋反
応を行い水不溶のゲルを濾取した。41 g of dry powder of Satsuma mandarin peel was subjected to Soxhlet extraction for about 6 hours using a 45% acetone aqueous solution heated to 60°C with 240 paper, and 28 g of acetone insoluble matter remained.
(mixed crystal) was collected by filtration. This is mixed with a 5:l (volume ratio) of 50% by weight acetone aqueous solution and epichlorohydrin.
50 d and maintained at 40°C under stirring. Next, 5M
50 d of NaOH was added thereto, a crosslinking reaction was carried out at 40''C for 2 hours, and the water-insoluble gel was collected by filtration.
水500d中にこれを加え、30分間煮沸後濾過して熱
水可溶成分を除去した。不溶物を送風乾燥機で乾燥後、
ペクチン酸セルロースゲル乾燥物23.0 gを得た。This was added to 500 d of water, boiled for 30 minutes, and then filtered to remove hot water soluble components. After drying the insoluble matter with a blow dryer,
23.0 g of dried cellulose pectate gel was obtained.
(収率11.5%)
(実施例1)
クリフロマイセス・フラギリスIFO1963培養液よ
りエンドポリガラクチュロナーゼ(以後、PGと略す。(Yield: 11.5%) (Example 1) Endopolygalacturonase (hereinafter abbreviated as PG) was obtained from Chryphromyces fragilis IFO1963 culture solution.
)を分離、精製する例を示す。) is shown below.
クリプロマイセス・フラギリスIF01963株を培養
後、遠心分離により菌体を除去し上澄みを得た。After culturing Cryplomyces fragilis strain IF01963, the bacterial cells were removed by centrifugation to obtain a supernatant.
木上清より、限外濃縮、イオン交喚クロマトグラフィー
により部分精製PGを得た。このものの全活性は134
.9units、比活性131.0units/mg
proteinであった。Partially purified PG was obtained from the wood supernatant by ultraconcentration and ion exchange chromatography. The total activity of this thing is 134
.. 9 units, specific activity 131.0 units/mg
It was protein.
架橋剤2.6モル/糖残基のペクチン酸セルロースゲル
を常法により調製し、0.5M NaC1を含む0.1
h酢酸緩衝液(pH4,5)で平衡化させた後、2.5
×40C1Oカラムを作成した。上記部分精製PG試料
をカラムに添加後、該緩衝液にて溶出させた。溶出液を
フラクションコレクターにて分画し、各々の酵素活性及
び蛋白含量(A210)を測定した。活性画分を合わせ
た後透析によりNaC1を除去し、精製PG液とした。A cellulose pectate gel containing 2.6 mol of cross-linking agent/sugar residue was prepared by a conventional method, and 0.1 mol containing 0.5 M NaCl was added.
h After equilibration with acetate buffer (pH 4, 5), 2.5
A x40C1O column was created. After adding the partially purified PG sample to the column, it was eluted with the buffer. The eluate was fractionated using a fraction collector, and the enzyme activity and protein content (A210) of each fraction were measured. After the active fractions were combined, NaCl was removed by dialysis to obtain a purified PG solution.
本液は全活性133.8υn1ts、比活性180.2
units/■proteinであり、回収率99.2
%、比活性上昇1.38倍であった。This solution has a total activity of 133.8υn1ts and a specific activity of 180.2
units/■protein, recovery rate 99.2
%, the increase in specific activity was 1.38 times.
(対照例1)
実施例1において用いた部分精製PG試料と同じものを
、あらかじめ0.5M NaC1を含む0.1M酢酸緩
衝液(pH4,5)にて平衡化させたセファデックスG
−75カラム(2,5X40C1)に通した後、実施例
1同様にして分析を行った。活性画分を合わせ、脱塩後
得られた試料の全活性は127.6units、比活性
177.5units/pg protelnであり、
回収率94.6%、比活性上昇1.35倍であった。(Control Example 1) The same partially purified PG sample used in Example 1 was prepared using Sephadex G that had been equilibrated in advance with 0.1M acetate buffer (pH 4, 5) containing 0.5M NaCl.
After passing through a -75 column (2,5×40C1), analysis was carried out in the same manner as in Example 1. The total activity of the sample obtained after combining the active fractions and desalting was 127.6 units, the specific activity was 177.5 units/pg proteln,
The recovery rate was 94.6%, and the specific activity increased by 1.35 times.
(実施例2)
実施例1において使用したペクチン酸セルロースカラム
に、分子量測定キット(ファルマシアLKB製、アルド
ラーゼ: MW 158,000、カタラーゼ:罪23
2.000、オブアルブミン:開43,000 、キモ
トリプシノーゲンA : MW 25,000 、リボ
ヌクレアーゼA : MW 13,700各50■/含
む)より、1Iniをカラム上端より注意深く添加した
後、0.1hNaC1を含む0.05M リン酸カリウ
ム緩衝液(pH6,8)にて流速1I11/winで?
容土された。フラクションコレクターにて2dずつ分取
し、蛋白含量(A28゜)を測定した。この結果を図に
示す。(Example 2) Molecular weight measurement kits (manufactured by Pharmacia LKB, aldolase: MW 158,000, catalase: Sin 23) were added to the cellulose pectate column used in Example 1.
After carefully adding 1 Ini from the top of the column, 0.1 hNaCl was added. Containing 0.05M potassium phosphate buffer (pH 6,8) at a flow rate of 1I11/win?
It was buried. A fraction of 2 d was collected using a fraction collector, and the protein content (A28°) was measured. The results are shown in the figure.
図から分かるように本ゲルのカラムを、あらかじめ検量
しておけば蛋白質等の水溶性高分子の分子量測定にも応
用が可能であることが分かった。As can be seen from the figure, it was found that this gel column can be applied to the measurement of the molecular weight of water-soluble polymers such as proteins if it is calibrated in advance.
第1図はペクチン酸セルロースゲルを用いた蛋白質の分
離を示す図である。FIG. 1 is a diagram showing the separation of proteins using pectate cellulose gel.
Claims (1)
特徴とする水溶性高分子物質の精製方法。[Claims] 1. A carrier for gel filtration containing pectic acid cellulose gel. 2. A method for purifying a water-soluble polymer substance, which comprises performing gel filtration using the carrier according to claim 1.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2082924A JPH03284693A (en) | 1990-03-31 | 1990-03-31 | Carrier for gel-filtration |
PCT/JP1990/001493 WO1991007427A1 (en) | 1989-11-16 | 1990-11-15 | Carrier for column chromatography, process for separating and purifying water-soluble polymeric substance using said carrier, novel pectic acid-cellulose gel and process for preparing the same, and adsorbent for affinity chromatography |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2082924A JPH03284693A (en) | 1990-03-31 | 1990-03-31 | Carrier for gel-filtration |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03284693A true JPH03284693A (en) | 1991-12-16 |
Family
ID=13787788
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2082924A Pending JPH03284693A (en) | 1989-11-16 | 1990-03-31 | Carrier for gel-filtration |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03284693A (en) |
-
1990
- 1990-03-31 JP JP2082924A patent/JPH03284693A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3002823A (en) | Process of separating materials having different molecular weights and dimensions | |
Hook et al. | Anticoagulant activity of heparin: separation of high-activity and low-activity heparin species by affinity chromatography on immobilized antithrombin | |
JPH07501937A (en) | Purified chitin deacetylase | |
JPH0353321B2 (en) | ||
CN102068965B (en) | Method for preparing chitosan separation medium suitable for protein purification | |
Lea et al. | Preparation of synthetic gels for chromatography of macromolecules | |
WO2007058592A1 (en) | A method of chromatography using semi-synthetic heparin ligands | |
US10527582B2 (en) | Use of stationary phase comprising fibril cellulose in separation methods | |
Fried et al. | [22] Water-soluble nonionic polymers in protein purification | |
CN101716494B (en) | Magnetic compatible microsphere for purifying thrombin and preparation method and application thereof | |
JPS6356501A (en) | Cellulose gel having biochemical affinity and production thereof | |
Turková et al. | Hydroxyalkyl methacrylate gels derivatized with epichlorohydrin as supports for large-scale and high-performance affinity chromatography | |
US4247452A (en) | Purification of pertussis haemagglutinins | |
Mårtensson et al. | Covalent coupling of pullulanase to an acrylic copolymer using a water soluble carbodi‐imide | |
US4990447A (en) | Process for the purification of serum albumin | |
Boschetti | Polyacrylamide derivatives to the service of bioseparations | |
DE69333185T2 (en) | DNA ENCODING CHITINE DEACETYLASE | |
EP0475383B1 (en) | Polysaccharide composition or polysaccharide having heparinoid activity, process for producing the same, and anticoagulant containing the same as active ingredient | |
JPH03284693A (en) | Carrier for gel-filtration | |
US3558433A (en) | Process for purification of chymopapain | |
Clapp et al. | Properties of extracellular polysaccharides from Rhizobium | |
JPS6154451A (en) | Gel for affinity chromatography having group specificity and its production | |
JP2903251B2 (en) | Carrier for affinity chromatography and method for purifying antithrombin III | |
WO1991007427A1 (en) | Carrier for column chromatography, process for separating and purifying water-soluble polymeric substance using said carrier, novel pectic acid-cellulose gel and process for preparing the same, and adsorbent for affinity chromatography | |
SU664967A1 (en) | Method of obtaining pectin |