JPH01265972A - Removing method of harmful component in humors - Google Patents
Removing method of harmful component in humorsInfo
- Publication number
- JPH01265972A JPH01265972A JP63273982A JP27398288A JPH01265972A JP H01265972 A JPH01265972 A JP H01265972A JP 63273982 A JP63273982 A JP 63273982A JP 27398288 A JP27398288 A JP 27398288A JP H01265972 A JPH01265972 A JP H01265972A
- Authority
- JP
- Japan
- Prior art keywords
- substance
- gel
- remove
- column
- affinity
- 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
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Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は体液中の有害成分の除去方法に関する。さらに
詳しくは、免疫疾患、腎炎、肝炎などの炎症、ウィルス
性疾患などにおいて、血液、血漿などの体液中に出現す
る有害物質、ウィルス、有害細胞などを吸着除去する方
法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for removing harmful components from body fluids. More specifically, the present invention relates to a method for adsorbing and removing harmful substances, viruses, harmful cells, etc. that appear in body fluids such as blood and plasma in immune diseases, inflammation such as nephritis and hepatitis, and viral diseases.
[従来の技術・発明が解決しようとする課題]人工透析
に端を発した体外循環治療は近年大いに発展し、治療対
象となる疾患も増加の一途をたどっている。これに伴い
、体液中に出現し、疾患の原因または進行と密接な関係
にあると考えられる有害成分をより選択的に除去する手
段が求められている。この目的のために膜による分離力
法が検討されてきたが、かかる方法は選択性が充分でな
く、除去対象物質以外の体液成分の損失が大きいという
欠点を有している。[Problems to be solved by conventional techniques and inventions] Extracorporeal circulation therapy, which originated from artificial dialysis, has developed greatly in recent years, and the number of diseases that can be treated is increasing. Along with this, there is a need for a means to more selectively remove harmful components that appear in body fluids and are thought to be closely related to the cause or progression of diseases. Separation force methods using membranes have been studied for this purpose, but such methods have the disadvantage of insufficient selectivity and large loss of body fluid components other than the substance to be removed.
また吸着により有害成分を除去しようとする試みがなさ
れ、活性炭、アンバーライトXADに代表される、いわ
ゆる合成吸着剤が主として肝臓病用に用いられてきてい
る。しかしながら、前記合成吸着剤は選択性に乏しく、
また高分子量物質は除去できないなど多くの欠点を有し
ている。Attempts have also been made to remove harmful components by adsorption, and so-called synthetic adsorbents, typified by activated carbon and Amberlite XAD, have been used mainly for liver diseases. However, the synthetic adsorbents have poor selectivity;
Furthermore, it has many drawbacks such as the inability to remove high molecular weight substances.
さらに選択性を高める目的で、水不溶性担体に除去対象
物質と親和性を有する物質を保持させた、いわゆるアフ
ィニティー吸着体を用いる試みが始められている。しか
しながら、これらの試みは通常アフィニティーク口マト
グラフィ−用に用いられる担体を転用したものが多く、
体外循環治療に用いるには好ましくない種々の欠点を有
していることが明らかとなっている。In order to further increase selectivity, attempts have been made to use so-called affinity adsorbents, in which a water-insoluble carrier holds a substance that has an affinity for the substance to be removed. However, many of these attempts have been based on repurposed carriers that are normally used for affinity stomatography.
It has become clear that it has various drawbacks that make it undesirable for use in extracorporeal circulation therapy.
すなわち、通常アフィニティークロマトグラフィーに用
いられる担体は、アガロース、デキストラン、ポリアク
リルアミド、多孔質ガラス、多孔質シリカなどであるが
、アガロース、デキストラン、ポリアクリルアミドなど
の軟質ゲルは、
(1)機械的強度が弱いため、撹拌などの操作により破
壊されやすい、
(2)耐圧強度が小さいため、カラムに充填して体外循
環に用いる際に高流速で体液を流すと圧密化をひきおこ
し、流速が安定せず、詰りを生じることもある
などの欠点を有している。That is, the carriers normally used for affinity chromatography are agarose, dextran, polyacrylamide, porous glass, porous silica, etc., but soft gels such as agarose, dextran, and polyacrylamide have (1) mechanical strength. Because it is weak, it is easily destroyed by operations such as stirring. (2) Because it has low pressure resistance, when body fluid is flowed at a high flow rate when packed in a column and used for extracorporeal circulation, it will cause compaction and the flow rate will not be stable. It has drawbacks such as clogging.
一方、多孔質ガラスなどの無機多孔体は耐圧強度は高い
ものの、
(1)撹拌などの操作により破壊されて微粉を生じやす
い、
(2)担体表面への除去対象物質以外の成分の吸着、い
わゆる非特異吸着が無視できないなどの欠点を有してい
る。On the other hand, although inorganic porous materials such as porous glass have high pressure resistance, (1) they are easily destroyed by operations such as stirring and produce fine powder, and (2) components other than the target substance are adsorbed onto the carrier surface, so-called It has drawbacks such as non-specific adsorption which cannot be ignored.
さらには、斜上の欠点を克服すべく合成高分子によるポ
リマーゲルが提案されているが、該欠点を充分克服して
いるとはいえず、未反応モノマーなどによる毒性も懸念
され、また吸着容量も軟質ゲルに劣っている。Furthermore, polymer gels made of synthetic polymers have been proposed to overcome the drawback of slanting, but these drawbacks cannot be said to be fully overcome, and there are concerns about toxicity due to unreacted monomers, and adsorption capacity. It is also inferior to soft gel.
[課mを解決するための手段]
本発明者らは斜上のごとき欠点を克服すべく鋭意研究を
重ねた結果、多孔質セルロースゲルに除去対象物質に親
和性を有する物質(以下、リガンドという)を保持させ
てなる吸着体と体液とを接触させることによって、高流
速で選択的に体液中の有害成分を吸着除去しうることを
見出し、本発明を完成するに至った。[Means for Solving Issue M] The present inventors have conducted intensive research to overcome the drawbacks such as slanting. As a result, the present inventors have injected a substance (hereinafter referred to as a ligand) that has an affinity for the substance to be removed into a porous cellulose gel. The present inventors have discovered that harmful components in body fluids can be selectively adsorbed and removed at a high flow rate by bringing an adsorbent holding body fluid into contact with body fluids, thereby completing the present invention.
すなわち、本発明に用いる多孔質セルロースゲルは、
(1)機械的強度が比較的高く、強じんであるため撹拌
などの操作により破壊されたり微粉を生じたりすること
が少ない、またカラムに充填して体液を高流速で流して
も圧密化したり目詰りしたりしないので、高流速で流す
ことが可能である、さらに細孔構造が高圧蒸気滅菌など
によって変化を受けにくい、
(2)ゲルがセルロースで構成されているため親水性で
あり、リガンドの結合に利用しうる水酸基が多数存在し
、非特異吸着も少ない、(3)空孔容積を大きくしても
比較的強度が高いため軟質ゲルに劣らない吸着容量かえ
られる、(4)安全性が合成高分子ゲルなどに比べて高
いなどの優れた点を有しており、該多孔質セルロースゲ
ルにリガンドを保持させることによって、はぼ理想的な
吸着体かえられ、この吸着体と体液とを接触させること
によって高流速で選択的に体液中の有害成分を吸着除去
しつる。In other words, the porous cellulose gel used in the present invention (1) has relatively high mechanical strength and is tough, so it is less likely to be destroyed or generate fine powder by operations such as stirring, and it can be packed into a column easily. (2) The gel is made of cellulose, so it does not become compacted or clogged even when body fluids are passed through it at high flow rates, so it is possible to flow at high flow rates. It is hydrophilic because it is composed of It has excellent features such as a comparable adsorption capacity and (4) higher safety than synthetic polymer gels.By retaining the ligand in the porous cellulose gel, it is ideal By bringing the adsorbent into contact with the body fluid, harmful components in the body fluid can be selectively adsorbed and removed at a high flow rate.
[実施例]
本発明に用いる多孔質セルロースゲルとしてはセルロー
ス自体のゲルが好ましいが、エステル化またはエーテル
化されたセルロース誘導体、あるいはセルロースと該誘
導体との混合物のゲルであってもよい。かかるセルロー
ス誘導体としてはアセチルセルロース、メチルセルロー
ス、エチルセルロース、カルボキシメチルセルロースな
どがあげられる。またゲル粒子の形態は球状が望ましい
。[Example] The porous cellulose gel used in the present invention is preferably a gel of cellulose itself, but may also be a gel of an esterified or etherified cellulose derivative, or a mixture of cellulose and the derivative. Examples of such cellulose derivatives include acetylcellulose, methylcellulose, ethylcellulose, and carboxymethylcellulose. Moreover, the shape of the gel particles is preferably spherical.
該多孔質セルロースゲルは、たとえばセルロースおよび
(または)セルロース誘導体を溶剤を用いて溶解あるい
は膨潤させたのち、用いた溶剤とは混和しない別の溶媒
中に分散させて球状とし、ゲル化再生する方法で製造す
ることができる。The porous cellulose gel can be produced by, for example, dissolving or swelling cellulose and/or cellulose derivatives using a solvent, then dispersing the cellulose and/or cellulose derivative in a different solvent that is immiscible with the used solvent to form spheres, and then gelling and regenerating the gel. It can be manufactured in
ゲルを構成するセルロースおよび(または)セルロース
誘導体は架橋されていてもよい。架橋剤の代表例として
は、エピクロルヒドリン、ジクロルヒドリン、ジェポキ
シ化合物、ジアルデヒド化合物、ジイソシアナート化合
物、塩化シアヌル、ジアルコキシアルキルシラン化合物
、トリアルコキシアルキルシラン化合物などがあげられ
るが、該架橋剤に限定されるわけではない。Cellulose and/or cellulose derivatives constituting the gel may be crosslinked. Typical examples of crosslinking agents include epichlorohydrin, dichlorohydrin, jepoxy compounds, dialdehyde compounds, diisocyanate compounds, cyanuric chloride, dialkoxyalkylsilane compounds, trialkoxyalkylsilane compounds, but are limited to these crosslinking agents. It's not like that.
本発明に用いる多孔質セルロースゲルの細孔径について
は、除去対象物質の分子量およびサイズにより最適のも
のを選ぶことができる。細孔径の測定法には種々のもの
があり、直接測定する方法としては水銀圧入法、電子顕
微鏡観察による方法などがあるが、含水粒子については
これらの方法を適用できないばあいがある。このような
場合には排除限界分子量を細孔径の目安とすることがで
きる。排除限界分子量とは底置(たとえば波多野博行、
花卉俊彦著、実験高速液体クロマトグラフ、化学同人)
などに述べられているように、ゲル浸透クロマトグラフ
ィーにおいて細孔内に侵入できない(排除される)分子
のうち最少の分子量を有するものの分子量のことである
。現象的には、排除限界分子量以上の分子量のものは移
動相体積近傍に溶出されることから、種々の分子量の化
合物を用いて溶出体積との関係を調べれば排除限界分子
量を求めることができる。The optimum pore diameter of the porous cellulose gel used in the present invention can be selected depending on the molecular weight and size of the substance to be removed. There are various methods for measuring pore diameter, and direct measurement methods include mercury porosimetry and electron microscopic observation, but these methods may not be applicable to water-containing particles. In such cases, the exclusion limit molecular weight can be used as a guideline for the pore diameter. What is the exclusion limit molecular weight (for example, Hiroyuki Hatano,
Written by Toshihiko Hana, Experimental High Performance Liquid Chromatograph, Chemistry Doujin)
As stated in et. Phenomenologically, molecules with molecular weights greater than the exclusion limit molecular weight are eluted near the volume of the mobile phase, so the exclusion limit molecular weight can be determined by examining the relationship with the elution volume using compounds of various molecular weights.
排除限界分子量は対象とする化合物の種類により異なっ
ており、本発明に用いる多孔質セルロースゲルは、球状
蛋白質およびウィルスを除去対象物質としたばあいの排
除限界分子量(以下、排除限界分子量という)は5X1
03〜1×108の範囲であることが好ましい。排除限
界分子量がIXLO8を超えるとリガンドの保持二が減
少して除去対象物質の吸着量が減り、またゲルの強度が
低下するため好ましくない。The exclusion limit molecular weight differs depending on the type of target compound, and the porous cellulose gel used in the present invention has an exclusion limit molecular weight (hereinafter referred to as exclusion limit molecular weight) of 5×1 when globular proteins and viruses are the substances to be removed.
The range is preferably from 0.03 to 1.times.10.sup.8. If the exclusion limit molecular weight exceeds IXLO8, it is not preferable because the retention of the ligand decreases, the adsorption amount of the substance to be removed decreases, and the strength of the gel decreases.
多孔質セルロースゲルの空孔容積はセルロース含量を目
安にすることができる。セルロース含量はつぎに示す式
で表わされる。The pore volume of the porous cellulose gel can be determined based on the cellulose content. The cellulose content is expressed by the formula shown below.
セルロース含量(%)−X100 Vt−V。Cellulose content (%)-X100 Vt-V.
(式中、Wはゲル重ffi(g) 、Vtはゲルを充填
したカラムの体積(ml)、Voはゲルの細孔に侵入し
えない高分子量物質をゲルが充填されたカラムに通した
ばあい、該高分子量物質がカラムから溶出するまでの溶
出容積(ml)である。)本発明に用いる多孔質セルロ
ースゲルはセルロース含量が2%以上60%以下である
ことが好ましく、2%より少ないとゲルの強度が低下し
、60%を超えると細孔容積が小さくなり好ましくない
。(In the formula, W is the gel weight ffi (g), Vt is the volume of the gel-filled column (ml), and Vo is the amount of high molecular weight substance that cannot enter the gel pores passed through the gel-filled column. (If the high molecular weight substance elutes from the column, it is the elution volume (ml).) The porous cellulose gel used in the present invention preferably has a cellulose content of 2% or more and 60% or less, and less than 2%. If it is less than 60%, the strength of the gel decreases, and if it exceeds 60%, the pore volume becomes small, which is not preferable.
多孔質セルロースゲルの粒子径は一般的には小さい方が
吸着能力の点で好ましいが、粒子径があまり小さくなる
とカラムなどに充填したばあいの圧力損失が大きくなる
ため好ましくなく、粒子径は1〜5,000μの範囲で
あることが好ましい。Generally, the smaller the particle size of the porous cellulose gel, the better from the viewpoint of adsorption capacity, but if the particle size becomes too small, the pressure loss will increase when packed in a column, etc., which is undesirable. Preferably, it is in the range of 5,000μ.
本発明に用いる除去対象物質に親和性を宵する物質(リ
ガンド)としてはつぎに示す物質が代表例としてあげら
れる。The following substances are representative examples of substances (ligands) that have an affinity for the substance to be removed used in the present invention.
免疫複合体を除去するには、C1,などの補体成分、プ
ロティンAなどの特異蛋白質、免疫複合体に対する抗体
などを用いることができる。To remove immune complexes, complement components such as C1, specific proteins such as protein A, antibodies against immune complexes, etc. can be used.
自己免疫疾患などで出現する自己抗体などを除去するに
は、たとえば全身性エリテマトーデスにおいて血中に出
現する抗核抗体や抗DNA抗体を除去するには、核酸塩
基、ヌクレオシド、ヌクレオチド、ポリヌクレオチド、
さらにはDNA 、 RNAなどを用いることができ、
重症筋無力症において出現する抗アセチルコリンリセプ
ター抗体を除去するには、アセチルコリンリセブター分
画成分を用いることができる。To remove autoantibodies that appear in autoimmune diseases, for example, to remove anti-nuclear antibodies and anti-DNA antibodies that appear in the blood in systemic lupus erythematosus, nucleobases, nucleosides, nucleotides, polynucleotides,
Furthermore, DNA, RNA, etc. can be used,
To remove anti-acetylcholine receptor antibodies that appear in myasthenia gravis, an acetylcholine receptor fraction component can be used.
そのほかにも自己抗体の除去には各自己抗体に対する抗
原を用いることができる。In addition, antigens for each autoantibody can be used to remove autoantibodies.
さらには、血中に出現する種々の有害成分を除去するた
めには、除去対象物質に対する抗体を用いることができ
る。たとえば、肝炎ウィルスの除去にはウィルス表面の
抗原に対する抗体、全身性エリテマトーデスにおいて血
中に出現するDNAなどの除去には抗DNA抗体などを
用いることができる。またリンパ球異常に対しては抗B
細胞抗体、抗すプレッサーT細胞体などを用いてリンパ
球を除去することもできる。Furthermore, in order to remove various harmful components that appear in the blood, antibodies against substances to be removed can be used. For example, antibodies against antigens on the surface of viruses can be used to remove hepatitis viruses, and anti-DNA antibodies can be used to remove DNA that appears in the blood in systemic lupus erythematosus. Anti-B for lymphocyte abnormalities
Lymphocytes can also be removed using cell antibodies, anti-pressor T cell bodies, and the like.
斜上のごとく抗原−抗体反応を利用する方法のほかに、
被吸着物質に特異的な親和性(アフィニティー)を有す
る物質を用いることができる。代表例としては、関節リ
ウマチ症において出現するリウマチ因子を除去するため
の変性あるいは凝集されたイムノグロブリン、γ −グ
ロブリンまたはそれらの分画成分、トリプトファンなど
のアミノ酸、リポ蛋白除去のためのヘパリンなどの硫酸
化多糖類、イムノグロブリン除去のためのプロティンA
1ハプトグロビン除去のためのヘモグロビン、プラスミ
ノゲン除去のためのリジン、C19除去のためのイムノ
グロブリンG1プレカリクレイン除去のためのアルギニ
ン、トランスコーチン除去のためのコーチゾル、ヘモベ
キシン除去のためのヘミン、エンドトキシン除去のため
のポリミキシンなどがあげられる。さらには、コンカナ
バリンA1コングルチニン、フィトヘマグルチニンなど
のレクチン、核酸、酵素、基質、補酵素なども用いるこ
とができる。In addition to methods using antigen-antibody reactions as shown above,
A substance having a specific affinity for the adsorbed substance can be used. Typical examples include denatured or aggregated immunoglobulins for removing rheumatoid factors that appear in rheumatoid arthritis, γ-globulin or their fractionated components, amino acids such as tryptophan, and heparin for removing lipoproteins. Protein A for removing sulfated polysaccharides and immunoglobulins
1 hemoglobin for haptoglobin removal, lysine for plasminogen removal, immunoglobulin G1 for C19 removal, arginine for prekallikrein removal, cortisol for transcotin removal, hemin for hemovexin removal, endotoxin removal Examples include polymyxins. Furthermore, lectins such as concanavalin A1 conglutinin and phytohemagglutinin, nucleic acids, enzymes, substrates, coenzymes, etc. can also be used.
以上に述べた除去対象物質およびリガンドはあくまで代
表例にすぎず、これらに限定されるわけではない。除去
対象物質としては、たとえば尿酸ビリルビンのように分
子ffi 1000以下のものから、たとえばウィルス
のように分子量数千万態上のものまで種々のものがあげ
られる。また担体の多孔質セルロースゲルは、通常除去
対象物質の分子量および分子サイズに応じて決定される
が、リガンドの種類、除去対象物質の分子の形状などに
よっても影響をうけ、たとえば除去対象物質の分子量が
数百、数百刃、数千刃のものに対してはそれぞれ排除限
界分子−が数千〜数十刃、数千刃、数千刃〜1億のもの
を用いるのが適当である。またリガンドは単独で用いて
もよいし、2種以上を混合して用いてもよい。The substances to be removed and the ligands described above are merely representative examples, and the present invention is not limited to these. The substances to be removed include a variety of substances, ranging from those with a molecular ffi of less than 1000, such as bilirubin urate, to those with a molecular weight of several tens of millions, such as viruses. In addition, the porous cellulose gel of the carrier is usually determined according to the molecular weight and molecular size of the substance to be removed, but it is also influenced by the type of ligand, the shape of the molecule of the substance to be removed, etc. For those with several hundred, several hundred, or several thousand blades, it is appropriate to use those with an exclusion limit molecule of several thousand to several tens of blades, several thousand blades, or several thousand blades to 100 million blades, respectively. Further, the ligands may be used alone or in combination of two or more types.
リガンドを担体の多孔質セルロースゲルに保持させる方
法には公知の種々の方法を用いることができる。すなわ
ち、物理的方法、イオン結合法、共有結合法などがあげ
られる。本発明の除去方法を体外循環治療に用いる際に
は、リガンドが脱離しないことが重要であるため結合の
強固な共有結合法が好ましく、その他の方法を用いるに
しても脱離を防ぐ工夫が必要である。Various known methods can be used to retain the ligand in the porous cellulose gel carrier. That is, physical methods, ionic bonding methods, covalent bonding methods, etc. can be mentioned. When using the removal method of the present invention for extracorporeal circulation treatment, it is important that the ligand does not detach, so a strong covalent bonding method is preferable, and even if other methods are used, measures to prevent detachment should be taken. is necessary.
また必要に応じてスペーサーを担体とリガンドの間に導
入してもよい。Furthermore, a spacer may be introduced between the carrier and the ligand if necessary.
前記吸着体と体液を接触させる手段としては種々のもの
があげられる。たとえば入口と出口に体液成分は通過す
るが吸着体は通過しないフィルター、メツシュなどを装
着したカラムに吸着体を充填し、該カラムを体外循環回
路に組み込み、血液、血漿などをカラムに通して行なう
体外循環治療に用いるのが代表的であるが、必ずしもか
かる手段に限定されるものではない。Various methods can be used for bringing the adsorbent into contact with body fluids. For example, an adsorbent is packed into a column equipped with a filter or mesh that allows body fluid components to pass through but not the adsorbent at the inlet and outlet, the column is installed in an extracorporeal circulation circuit, and blood, plasma, etc. are passed through the column. Although it is typically used for extracorporeal circulation therapy, it is not necessarily limited to such means.
前記吸着体はリガンドが大幅に変性されない限り、高圧
蒸気滅菌が可能であり、該滅菌操作による細孔、粒子の
形状、体積の変化はわずかである。The adsorbent can be sterilized by high-pressure steam as long as the ligand is not significantly denatured, and the sterilization process causes only slight changes in the shape and volume of the pores and particles.
つぎに実施例をあげて本発明をさらに詳しく説明するが
、本発明はかかる実施例のみに限定されるものではない
。Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited to these Examples.
実施例1
セルロファインA−3(チッソ■製の多孔質セルロース
ゲル、排除限界分子量5X107、粒子径45〜105
場) lomlに20%NaOH4g 、ヘプタン12
g1ノニオン系界面活性剤トウィーン20(Tween
20)を1滴加え、40℃で2時間攪拌後、エピクロル
ヒドリン5gを加えて2時間攪拌した。静置後上澄みを
捨て、ゲルを水洗濾過してエポキシ化セルロースゲルを
えた。えられたゲルに濃アンモニア水15m1加え、4
0°Cで1.5時間攪拌し、内容物を吸引濾過し、水洗
してアミノ基の導入されたセルロースゲルをえた。Example 1 Cellulofine A-3 (Porous cellulose gel manufactured by Chisso ■, exclusion limit molecular weight 5X107, particle size 45-105
20% NaOH 4g, heptane 12 in loml
g1 Nonionic surfactant Tween 20
20) was added, and the mixture was stirred at 40°C for 2 hours, and then 5 g of epichlorohydrin was added and stirred for 2 hours. After standing still, the supernatant was discarded, and the gel was washed with water and filtered to obtain an epoxidized cellulose gel. Add 15ml of concentrated ammonia water to the resulting gel,
The mixture was stirred at 0°C for 1.5 hours, and the contents were suction filtered and washed with water to obtain a cellulose gel into which amino groups had been introduced.
つぎにヘパリン200 mgを水10m1に溶解し、こ
れに前記アミノ基含有ゲル3 mlを加え、pl+4.
5に調整したのち、1−エチル−3−(ジメチルアミノ
プロピル)−カルボジイミド200 mgをpH4,5
に保ちながら添加し、4°Cで24時間振とうした。Next, 200 mg of heparin was dissolved in 10 ml of water, and 3 ml of the amino group-containing gel was added thereto to give a solution of pl+4.
5, then 200 mg of 1-ethyl-3-(dimethylaminopropyl)-carbodiimide was adjusted to pH 4.5.
The mixture was added while maintaining the temperature at 4°C, and was shaken for 24 hours at 4°C.
反応終了後、2M食塩水溶液、0.5M食塩水溶液およ
び水で洗浄してヘパリンの保持されたセルロースゲルを
えた。保持されたヘパリン量は1 、8mg / ml
であった。またここまでの操作によりゲルが破壊された
り、微粉の発生は認められなかった。After the reaction was completed, the gel was washed with a 2M saline solution, a 0.5M saline solution, and water to obtain a cellulose gel retaining heparin. The amount of heparin retained was 1.8 mg/ml
Met. Furthermore, no breakage of the gel or generation of fine powder was observed during the operations up to this point.
ついでえられた吸着体を内径91IIII11長さ47
止、内容積約3 mlのカラムに充填し、高脂血症患者
の血漿18m1を0.3ml/分でカラムに通した。カ
ラムでの圧力損失は終始15m+s)1g以下で、目詰
りなどは観察されなかった。Next, the obtained adsorbent has an inner diameter of 91III, 11 and a length of 47.
A column having an internal volume of approximately 3 ml was filled with the sample, and 18 ml of plasma from a hyperlipidemic patient was passed through the column at a rate of 0.3 ml/min. The pressure loss in the column was less than 1 g (15 m+s) throughout, and no clogging was observed.
カラムを通過させることにより血漿中の総コレステロー
ルの65%が吸着され、総蛋白などの減少はわずかであ
った。By passing through the column, 65% of the total cholesterol in plasma was adsorbed, and total protein etc. decreased only slightly.
実施例2
実施例1で用いたセルロファインA−3の粒子径を15
0〜200μにかえたほかは実施例1と同様にしてヘパ
リンの保持されたセルロースゲルをえた。保持されたヘ
パリン量は1 、5mg / mlであった。Example 2 The particle size of Cellulofine A-3 used in Example 1 was changed to 15
A heparin-retained cellulose gel was obtained in the same manner as in Example 1 except that the thickness was changed from 0 to 200μ. The amount of heparin retained was 1.5 mg/ml.
斜上のゲルを実施例1と同じカラムに充填し、高脂血症
患者の血漿18m1(ヘパリン200U添加)を0.2
ml/分でカラムに通した。カラムでの圧力損失は30
mmHg以下であり、変化もわずかであった。Fill the top gel into the same column as in Example 1, and add 18 ml of plasma from a hyperlipidemic patient (added with 200 U of heparin) to 0.2
Passed through the column at ml/min. The pressure drop in the column is 30
It was below mmHg, and the change was slight.
カラムを通過させることにより血漿中の総コレステロー
ルの55%が吸着され、総蛋白、血球の減少はわずかで
あった。また吸着体表面での血栓形成もわずかであった
。By passing through the column, 55% of the total cholesterol in plasma was adsorbed, and there was only a slight decrease in total protein and blood cells. Furthermore, there was little thrombus formation on the adsorbent surface.
実施例3
実施例1でえられたヘパリンの保持されたゲルをオート
クレーブを用いて120℃で15分間滅菌し、実施例1
と同じカラムに充填し、高脂血症患者の血漿18m1を
0.3ml/分でカラムに通した。カラムでの圧力損失
、総コレステロールの吸着はともに実施例1と同様であ
った。Example 3 The heparin-retained gel obtained in Example 1 was sterilized using an autoclave at 120°C for 15 minutes, and the heparin-retained gel obtained in Example 1 was
18 ml of plasma from a hyperlipidemic patient was passed through the column at 0.3 ml/min. Both the pressure drop in the column and the adsorption of total cholesterol were the same as in Example 1.
実施例4
実施例1と同様にしてエポキシ化セルロースゲルを作製
した。えられたゲル10m1にプロティンA50ff1
gを加え、pH9,5に調整し、室温で24時間反応さ
せたのち、2M食塩水溶液、0.5M食塩水溶液および
水で洗浄した。ついでモノエタノールアミンを加え、1
6時間反応させて未反応エポキシ基を封止し、ついで水
洗してプロティンAの保持されたセルロースゲルをえた
。Example 4 An epoxidized cellulose gel was produced in the same manner as in Example 1. Add 50ff1 of protein A to 10ml of the resulting gel.
After adjusting the pH to 9.5 and reacting at room temperature for 24 hours, the mixture was washed with a 2M saline solution, a 0.5M saline solution, and water. Then add monoethanolamine and add 1
The mixture was reacted for 6 hours to seal unreacted epoxy groups, and then washed with water to obtain a cellulose gel in which protein A was retained.
えられた吸着体を実施例1と同じカラムに充填し、ヒト
血漿18m1を0.3ml/分でカラムに通したところ
、約35%のグロブリンが吸着された。When the obtained adsorbent was packed into the same column as in Example 1 and 18 ml of human plasma was passed through the column at 0.3 ml/min, about 35% of globulin was adsorbed.
なお、アルブミンの減少はわずかであった。Note that the decrease in albumin was slight.
実施例5
実施例1で用いたセルロファインA−3の20 mlを
水に分散させ、これにplを11〜12に保ちながら臭
化シアン6gを徐々に添加し、10分間攪拌した。ゲル
を決別し、冷水およびO,1MNaHcO3水溶液で洗
浄して活性化ゲルをえた。ついでポリミキシン硫酸塩1
.5gを0.IMNallCO3水溶液20m1に溶解
し、これに斜上のゲルを加えて4℃で24時間振とうし
たのち、モノエタノールアミン溶液を用いて過剰の活性
基を封止してポリミキシンの保持されたセルロースゲル
をえた。Example 5 20 ml of Cellulofine A-3 used in Example 1 was dispersed in water, and 6 g of cyanogen bromide was gradually added thereto while maintaining the PL at 11 to 12, followed by stirring for 10 minutes. The gel was broken off and washed with cold water and O, 1M NaHcO3 aqueous solution to obtain an activated gel. Then polymyxin sulfate 1
.. 5g to 0. After dissolving in 20 ml of IMNallCO3 aqueous solution and adding the top gel to this and shaking at 4°C for 24 hours, excess active groups were sealed using a monoethanolamine solution to form a cellulose gel with polymyxin retained. I got it.
えられたゲル1 mlを内径7 mmのオーブンカラム
に充填し、エンドトキシン添加(約100μg/ ml
)牛血類5 mlを0.3ml/分でカラムに通した
ところ、60%のエンドトキシンが吸着された。1 ml of the resulting gel was packed into an oven column with an inner diameter of 7 mm, and endotoxin was added (approximately 100 μg/ml).
) When 5 ml of bovine blood was passed through the column at 0.3 ml/min, 60% of endotoxin was adsorbed.
実施例6
セルロフアインA−3をセルロファインA−2(チッソ
沖製の多孔質セルロースゲル、排除限界分子=7xto
s、粒子径45〜1105AI〉にかえたほかは実施例
1と同様にしてエポキシ化セルロースゲルを作製した。Example 6 Cellulofine A-3 was mixed with Cellulofine A-2 (porous cellulose gel manufactured by Chisso Oki, exclusion limit molecule = 7xto
An epoxidized cellulose gel was produced in the same manner as in Example 1 except that the particle size was changed to 45 to 1105 AI.
えられたゲル10m1にヒトイムノグロブリン010m
gを加え、pH9,0に調整し、室温で24時間反応さ
せたのち、ゲルを決別し、2M食塩水溶液、0.5M食
塩水溶液および水で洗浄した。ついでモノエタノールア
ミン溶液を用いて未反応エポキシ基を封止してイムノグ
ロブリンGの保持されたセルロースゲルをえlこ 。0.10ml of human immunoglobulin was added to 10ml of the resulting gel.
After adjusting the pH to 9.0 and reacting at room temperature for 24 hours, the gel was separated and washed with a 2M saline solution, a 0.5M saline solution, and water. Next, unreacted epoxy groups were sealed using a monoethanolamine solution, and the cellulose gel in which immunoglobulin G was retained was removed.
つぎにえられたゲルを実施例1と同じカラムに充填し、
ヒト血漿18m1を0.2ml/分でカラムに通したと
ころ、約30%の019が吸着された。Next, the obtained gel was packed into the same column as in Example 1,
When 18 ml of human plasma was passed through the column at 0.2 ml/min, about 30% of 019 was adsorbed.
[発明の効果]
本発明の方法によれば、体液中の宵害成分を選択的に除
去することができる。また、本発明の方法を、吸着体を
カラムに充填し、体液を高流速で流す体外循環治療に適
用すると、吸着剤の圧密化、目詰りおよび破壊がおこり
にくいので、安全に効率よく有害成分を除去することが
できる。[Effects of the Invention] According to the method of the present invention, harmful components in body fluids can be selectively removed. Furthermore, when the method of the present invention is applied to extracorporeal circulation therapy in which an adsorbent is packed into a column and body fluids are passed through at a high flow rate, the adsorbent is less likely to become compacted, clogged, or destroyed, so harmful substances can be removed safely and efficiently. can be removed.
Claims (1)
する物質が保持されてなる吸着体と体液とを接触させる
ことを特徴とする体液中の有害成分の除去方法。1. A method for removing harmful components in body fluids, which comprises bringing body fluids into contact with an adsorbent in which a porous cellulose gel holds a substance that has an affinity for the substance to be removed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63273982A JPH01265972A (en) | 1988-10-29 | 1988-10-29 | Removing method of harmful component in humors |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63273982A JPH01265972A (en) | 1988-10-29 | 1988-10-29 | Removing method of harmful component in humors |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58068116A Division JPS59193135A (en) | 1982-12-02 | 1983-04-18 | Adsorbing body |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01265972A true JPH01265972A (en) | 1989-10-24 |
Family
ID=17535288
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63273982A Pending JPH01265972A (en) | 1988-10-29 | 1988-10-29 | Removing method of harmful component in humors |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01265972A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997047969A1 (en) * | 1996-06-10 | 1997-12-18 | Precision System Science Co., Ltd. | Fine substance hold-back carrier, suspension system for the same, fine substance manipulating apparatus and method of controlling position of fine substance |
WO2002090990A1 (en) * | 2001-05-09 | 2002-11-14 | Kyowa Medex Co., Ltd. | Biopolymer-containing gel |
JP2008513771A (en) * | 2004-09-22 | 2008-05-01 | ジーイー・ヘルスケア・バイオサイエンス・アクチボラグ | Method for producing chromatography matrix |
JP2010260052A (en) * | 2010-07-27 | 2010-11-18 | Kuraray Medical Inc | Adsorbing material for recovering blood component |
JP2013010701A (en) * | 2011-06-28 | 2013-01-17 | Jnc Corp | Endotoxin adsorbent,column for whole blood perfusion type extracorporeal circulation using the same, and chromatography filler for purifying pharmaceutical drug |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57156035A (en) * | 1981-03-24 | 1982-09-27 | Asahi Chem Ind Co Ltd | Adsorbent and adsorbing device for immune conjugated substance |
JPS587256A (en) * | 1981-07-06 | 1983-01-17 | テルモ株式会社 | Immune control substance des-i removing agent used in body liquid |
JPS5861752A (en) * | 1981-10-08 | 1983-04-12 | 旭化成株式会社 | Material and apparatus for adsorbing malodorous substance |
-
1988
- 1988-10-29 JP JP63273982A patent/JPH01265972A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57156035A (en) * | 1981-03-24 | 1982-09-27 | Asahi Chem Ind Co Ltd | Adsorbent and adsorbing device for immune conjugated substance |
JPS587256A (en) * | 1981-07-06 | 1983-01-17 | テルモ株式会社 | Immune control substance des-i removing agent used in body liquid |
JPS5861752A (en) * | 1981-10-08 | 1983-04-12 | 旭化成株式会社 | Material and apparatus for adsorbing malodorous substance |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997047969A1 (en) * | 1996-06-10 | 1997-12-18 | Precision System Science Co., Ltd. | Fine substance hold-back carrier, suspension system for the same, fine substance manipulating apparatus and method of controlling position of fine substance |
US7071006B2 (en) | 1996-06-10 | 2006-07-04 | Precision System Science Co., Ltd. | Carrier holding micro-substances, system suspending such carriers apparatus for manipulating such carriers and method of controlling positions of such carriers |
WO2002090990A1 (en) * | 2001-05-09 | 2002-11-14 | Kyowa Medex Co., Ltd. | Biopolymer-containing gel |
JP2008513771A (en) * | 2004-09-22 | 2008-05-01 | ジーイー・ヘルスケア・バイオサイエンス・アクチボラグ | Method for producing chromatography matrix |
JP2010260052A (en) * | 2010-07-27 | 2010-11-18 | Kuraray Medical Inc | Adsorbing material for recovering blood component |
JP2013010701A (en) * | 2011-06-28 | 2013-01-17 | Jnc Corp | Endotoxin adsorbent,column for whole blood perfusion type extracorporeal circulation using the same, and chromatography filler for purifying pharmaceutical drug |
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