JPS5827559A - Low density lipoprotein adsorbent - Google Patents

Low density lipoprotein adsorbent

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Publication number
JPS5827559A
JPS5827559A JP56126443A JP12644381A JPS5827559A JP S5827559 A JPS5827559 A JP S5827559A JP 56126443 A JP56126443 A JP 56126443A JP 12644381 A JP12644381 A JP 12644381A JP S5827559 A JPS5827559 A JP S5827559A
Authority
JP
Japan
Prior art keywords
low
pore diameter
adsorbent
sulfonic acid
density lipoprotein
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
Application number
JP56126443A
Other languages
Japanese (ja)
Inventor
正夫 谷原
俊秀 中島
高倉 孝一
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.)
Kuraray Co Ltd
Original Assignee
Kuraray 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 Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP56126443A priority Critical patent/JPS5827559A/en
Publication of JPS5827559A publication Critical patent/JPS5827559A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、高コレステロール患者血液中のコレステロー
ルを大量に含んだ低密度リポ蛋白質を除去できる吸着剤
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an adsorbent capable of removing low-density lipoproteins containing a large amount of cholesterol from the blood of patients with high cholesterol.

高コレステロール血症、特に家族性高コレスプロール血
症は遺伝的に細胞膜の低密18°リボ蛋白質リセブター
の欠損により、血中コレステロール博度が高く、血管壁
へのコレステロールの沈漬により動脈硬化を引き起こし
、さらには心筋梗塞や狭心症により死亡する率の高い疾
患である。そこでこれらの患者の血液中のコレステロー
ルを人けに含A、だ低密度リポ蛋白質を除去する必萼が
ある。
Hypercholesterolemia, especially familial hypercholesterolemia, is caused by a genetic defect in the low-density 18° riboprotein receptor in cell membranes, resulting in a high level of cholesterol in the blood, which causes arteriosclerosis due to deposition of cholesterol in blood vessel walls. It is a disease with a high rate of death due to myocardial infarction and angina pectoris. Therefore, it is necessary to remove cholesterol and low-density lipoproteins from the blood of these patients.

従来、血漿交換法等が施行されでいたが、毎回補充する
血漿が高価で品不足であるという問題点がある。
Conventionally, methods such as plasma exchange have been implemented, but there are problems in that the plasma that needs to be replenished each time is expensive and in short supply.

吸着法は、選択的にコレステロール、あるいは低密度リ
ポ蛋白質を除去できnば補液が要らないという長所があ
り、ヘパリンを固定化したアガロース (80Moor
jat++  ら、Cl1n、  Chiru、  A
cta 77(1977)21−30.)が使われ、効
果があることが報告されているだけである。しかしなが
ら担体であるアガロースが機械的に弱く、又血液凝固因
子をも同時に吸着するという問題点があった。
The adsorption method has the advantage of not requiring fluid replacement if it can selectively remove cholesterol or low-density lipoproteins.
jat++ et al., Cl1n, Chiru, A.
cta 77 (1977) 21-30. ) have been used and reported to be effective. However, there was a problem that the carrier, agarose, was mechanically weak and also adsorbed blood coagulation factors at the same time.

本発明者らはこれらの事情に艦み鋭意研究を重ねた結果
、表面に特定の官能基を有し、かつ特定の平均細孔直径
を持つ多孔体が血漿中の低密度リポ蛋白質(したがって
コレステロール)を選択的に減少させることを見出し、
本発明を完成させるに到った。即ち本発明は、表面にス
ルホン酸基を有し、かつ平均細孔直径が700〜200
0Aの範囲内にある多孔体であることを特徴とする低密
度リポ蛋白質吸着剤である。
As a result of intensive research into these circumstances, the present inventors found that a porous material having a specific functional group on its surface and a specific average pore diameter was able to absorb low-density lipoproteins in plasma (and therefore cholesterol). ) was found to selectively decrease
The present invention has now been completed. That is, the present invention has a sulfonic acid group on the surface and an average pore diameter of 700 to 200.
This is a low-density lipoprotein adsorbent characterized by being a porous material within the range of 0A.

本発明の吸着剤の表面にはスルホン酸基(−80sH,
−80g−)が存在することが必要である。
The surface of the adsorbent of the present invention has sulfonic acid groups (-80sH,
-80g-) is required.

ここで表面とは外表面と吸着剤の細孔の内部表面をも含
んだ全表面を言う。スルホン酸基を有する吸着剤には選
択的に低密度リボ蛋白質が吸着するが、カルボキシル基
やシラノール基等ではそれ程選択性が高くない理由は明
らかではないが、低密度リポ蛋白質にスルホン酸基と特
異的に結合するサイトが存在していると考えられる。ス
ルホン酸基の濃度は、5〜100μmo l /fの範
囲が好ましい。
Here, the surface refers to the entire surface including the outer surface and the inner surface of the pores of the adsorbent. Low-density riboproteins are selectively adsorbed to adsorbents with sulfonic acid groups, but it is not clear why the selectivity is not as high for carboxyl groups, silanol groups, etc.; It is thought that a specific binding site exists. The concentration of sulfonic acid groups is preferably in the range of 5 to 100 μmol/f.

濃度が5μmad/fより低くなると、効果が充分でな
くなる傾向が認められるようになり、また100μmo
17’ffを越えると効果が飽和して濃度を高めでもそ
れに対応した高い効果が得られなくなる傾向がでてくる
When the concentration is lower than 5μmad/f, there is a tendency that the effect is not sufficient, and when the concentration is lower than 5μmad/f,
When the concentration exceeds 17'ff, the effect tends to be saturated and even if the concentration is increased, a correspondingly high effect cannot be obtained.

スルホン酸基の導入方法としではシランカップリング剤
等を用いて化学結合により導入−(る方法、スルホン酸
基を含む重合体で被覆する万f1:等がある。化学結合
法は、例えば多孔体担体の表面に5−アミノプロピル゛
トリエトキシシランを反喧させでアミノ基を導入し、さ
らに酸性溶液中でグルタルアルデヒドを反応させ、次に
塩基性溶液中でタウリンを反応させる方法等がある。重
合体被覆によるスルホン酸基の導入はスルホン酸基を自
する重合体(例えはスチレンスルホン酸の重合体父はス
チレンスルホン酸を共重合成分としで含む重合体)で被
覆することにより実施できる。被覆7f法としでは単量
体を、必要ならば重合開始剤とともに溶解した溶液で被
覆した後加熱重合等により重合する方法を用いることが
できる。
Examples of methods for introducing sulfonic acid groups include a method of introducing them through chemical bonding using a silane coupling agent, and a method of coating the material with a polymer containing a sulfonic acid group. There is a method of introducing amino groups onto the surface of the carrier by stirring 5-aminopropyltriethoxysilane, reacting with glutaraldehyde in an acidic solution, and then reacting with taurine in a basic solution. Introduction of sulfonic acid groups by polymer coating can be carried out by coating with a polymer having sulfonic acid groups (for example, a polymer containing styrene sulfonic acid as a copolymer component of styrene sulfonic acid). As the coating method 7f, a method can be used in which a monomer is coated with a solution containing a polymerization initiator, if necessary, and then polymerized by heating polymerization or the like.

スルホン酸基を導入する担体としては多孔性ガラス、多
孔性シリカ、多孔性アルミナ、多孔性シリカ−アルミナ
等を用いることができるが、多孔性ガラスが物理的強度
が高く、好ましく使用される。
Porous glass, porous silica, porous alumina, porous silica-alumina, etc. can be used as the carrier to introduce the sulfonic acid group, but porous glass has high physical strength and is preferably used.

低密度リボ蛋白質は分子量が数百万の球状蛋白質である
ので、吸着剤の平均細孔直径は700A以上であること
が必要であり、900λ以上であることが、さらに好ま
しい。700ム以下の細孔には低密度リポ蛋白質は吸着
さnulB<、またr−グロブリン等の他の蛋白質も吸
着されるので好ましくない。したがって、スルホン酸基
を持つカチオン交換樹脂のように平均細孔直径が非常に
小さい(801以下)ものは、低密度リポ蛋白質が細孔
内に入ることができずほとんど吸着されないので不適当
である。平均細孔直径が2000A以上になると物理的
強度が低下して微細片を生じ易くなるので好ましくない
。平均細孔直径は1600λ以下であることがさらに好
ましい。
Since low-density riboprotein is a globular protein with a molecular weight of several million, the average pore diameter of the adsorbent needs to be 700A or more, and more preferably 900λ or more. Low-density lipoproteins are adsorbed to pores of 700 μm or less, and other proteins such as r-globulin are also adsorbed, which is not preferable. Therefore, cation exchange resins with a very small average pore diameter (801 or less), such as cation exchange resins with sulfonic acid groups, are unsuitable because low-density lipoproteins cannot enter the pores and are hardly adsorbed. . If the average pore diameter exceeds 2000 A, it is not preferable because the physical strength decreases and fine pieces are likely to occur. More preferably, the average pore diameter is 1600λ or less.

蛋白質を選択的に吸着するため吸着剤の細孔径分布が狭
いことが好ましく、平均細孔直径をDとするとき、細孔
11径が0.8D〜1.2Dの範囲内にある細孔の容積
の割合が全細孔容積の80%以上を占めることが好まし
い。
In order to selectively adsorb proteins, it is preferable that the pore size distribution of the adsorbent is narrow, and when the average pore diameter is D, the diameter of pores 11 is within the range of 0.8D to 1.2D. It is preferable that the volume ratio accounts for 80% or more of the total pore volume.

また、吸着剤の細孔容積1.i 0.5 cc/f 〜
2.0 cc/ fの範囲内にあることが好ましい。0
.5 cc/f以下では蛋白質の吸着容量が低く、本発
明の目的に適さなくなる。2. Occ/f以上では骨
格が脆弱化しで、微細破片が生じやすくなる。
In addition, the pore volume of the adsorbent is 1. i 0.5 cc/f ~
It is preferably within the range of 2.0 cc/f. 0
.. If it is less than 5 cc/f, the protein adsorption capacity will be low and it will not be suitable for the purpose of the present invention. 2. If it exceeds Occ/f, the skeleton becomes brittle and minute fragments are likely to occur.

本発明において使用される吸着剤は血液あるいは血漿等
の体液と接触させるため、粒子の直径が0.1−〜51
111の範囲内にあることが好ましく、0.2W1〜2
■の範囲にあることがさらに好ましい。粒径が0.1.
より小さくなると吸着体層の圧損が大きくなり、溶血等
の問題が生じる。粒径が5mより大きいと粒子間の空隙
が大きくなり、吸着性能が低下し好ましくない。
Since the adsorbent used in the present invention is brought into contact with body fluids such as blood or plasma, the particle diameter is 0.1-51.
It is preferably within the range of 111, and 0.2W1 to 2
It is more preferable to fall within the range (2). Particle size is 0.1.
If the size is smaller, the pressure drop in the adsorbent layer will increase, causing problems such as hemolysis. If the particle size is larger than 5 m, the voids between the particles will become large and the adsorption performance will deteriorate, which is not preferable.

また本吸着剤は血液と接触させるため血球成分に対する
安全性を高め、また凝血等を防ぐため球状の外形のもの
が好ましい。
Further, since the present adsorbent is brought into contact with blood, it is preferable to have a spherical external shape in order to increase the safety against blood cell components and to prevent blood clots and the like.

これらの吸着剤はそのまま用いても良いが、血液との親
和性を向上させるために表面を親水性重合体で被覆処理
して使用することもできる。親水性重合体の被覆方法と
しでは、多孔体を親水性重合体溶液に浸漬した後、溶媒
を除去する方法が好ましい。このような方法によれば、
親水性重合体は多孔体の細孔内にほとんど侵入しないの
で、細孔内表面のスルホン酸基が親水性重合体により被
覆されて機能が低下することはほとんどない。また、親
水性重合体としては架橋成分を含む重合体が好ましく、
被覆処理後、加熱して架橋させることがさらに好ましい
。親水性重合体の例としでは、アクリル酸エステル系重
合体、メタクリル酸エステル系重合体、アクリルアミド
系重合体、ポリビニルアルコール系重合体、ポリビニル
ピロリドン硝酸ヤルロース及びゼラチン等をあげること
ができる。
These adsorbents may be used as they are, but their surfaces may be coated with a hydrophilic polymer to improve their affinity with blood. As a method for coating with a hydrophilic polymer, a method is preferred in which the porous body is immersed in a hydrophilic polymer solution and then the solvent is removed. According to this method,
Since the hydrophilic polymer hardly penetrates into the pores of the porous body, there is almost no possibility that the sulfonic acid groups on the inner surface of the pores will be covered with the hydrophilic polymer and the functionality will deteriorate. In addition, as the hydrophilic polymer, a polymer containing a crosslinking component is preferable,
It is more preferable to heat and crosslink after the coating treatment. Examples of the hydrophilic polymer include acrylic ester polymers, methacrylic ester polymers, acrylamide polymers, polyvinyl alcohol polymers, polyvinylpyrrolidone yalulose nitrate, and gelatin.

に充填して使用される。カラムは吸着剤層の両側に血液
回路と容易に接続し得る形状の入口部と出口部を有する
本体と、吸着剤層と出入口部との間に、血液等は通過す
るが吸着剤は通過しない80〜180メツシ、1の網目
を持つフィルターを備えているものが好ましいが、他の
形状であっても実質的に同様の機能を持つカラムであれ
ば本目的に使用し得る。カラムの材質はガラス、ポリエ
チレン。
It is used by filling. The column has a main body having an inlet and an outlet shaped to be easily connected to a blood circuit on both sides of an adsorbent layer, and a space between the adsorbent layer and the inlet and outlet, through which blood, etc. passes, but the adsorbent does not pass through. A column having a filter having a mesh size of 80 to 180 mesh is preferable, but columns having other shapes having substantially the same function can be used for this purpose. The material of the column is glass and polyethylene.

ポリプロピレン、ポリカーボネート、ポリスチレン、ポ
リメチルメタクリレート等が使用できるがオートクレー
ブ滅菌が可能なポリプロピレンやポリカーボネート等が
好ましい。フィルターは生理学的に不活性で強度の高い
ものであれば良いが、特にポリエステル製のものが好ま
しい。
Polypropylene, polycarbonate, polystyrene, polymethyl methacrylate, etc. can be used, but polypropylene, polycarbonate, etc., which can be sterilized by autoclaving, are preferable. The filter may be made of any physiologically inert and strong material, but one made of polyester is particularly preferred.

本発明の吸着剤を充填したカラムは通常滅菌しで使用さ
れ、オートクレーブ滅菌、ri!滅菌が好ましい。
The column packed with the adsorbent of the present invention is normally used after being sterilized, such as autoclave sterilization, ri! Sterilization is preferred.

本発明の吸着剤は、全面をそのまま接融させることもで
きるが、あらかじめ血漿分離装置等で分離した血漿tご
けを接触させても良い。
The entire surface of the adsorbent of the present invention can be directly fused, but it may also be brought into contact with plasma sludge that has been separated in advance using a plasma separator or the like.

以F実施例により本発明をさらに具体的に説明するが、
本発明はかかる実施例に限定されるものではない。
Hereinafter, the present invention will be explained in more detail with reference to Examples.
The present invention is not limited to such embodiments.

実施例1〜4.比較例1〜5 平均細孔直径が720λの多孔性ガラス(k720λ、
細孔直径が0.8D〜1.2Dにある細孔容積の割合9
9%、細孔容積3.95cc/f、粒径0.2m〜o、
s、)を比較例1とし、これを5−アミノプロピルトリ
エトキシシランとトルエン中で加熱してアミノ基を導入
し、次に1規定塩酸中でグルタルアルデヒドと室温で1
2時間反応させ、次にタウリンと1規定水酸化すl−I
Jウム水溶液中で、室温で12時間反応させて55.1
μmol / fのスルホン酸基を導入した多孔性ガラ
スを実施例1として使用した。
Examples 1-4. Comparative Examples 1 to 5 Porous glass with an average pore diameter of 720λ (k720λ,
Percentage of pore volume with pore diameter between 0.8D and 1.2D9
9%, pore volume 3.95 cc/f, particle size 0.2 m~o,
Comparative Example 1 was prepared using Comparative Example 1. It was heated with 5-aminopropyltriethoxysilane in toluene to introduce an amino group, and then heated with glutaraldehyde in 1N hydrochloric acid at room temperature.
React for 2 hours, then taurine and 1N hydroxide l-I
55.1 by reacting for 12 hours at room temperature in a Jium aqueous solution.
A porous glass introduced with μmol/f of sulfonic acid groups was used as Example 1.

平均細孔径が1060λの多孔性ガラス(n=1060
^、細孔直径が0.8D〜1.2Dにある細孔容積の割
合81%、細孔容積0.92cc/p、粒径0.2劃〜
0.5m)を比較例2とし、これに実施例1と同様の方
法で54.5μmol/fのスルホン酸基を導入したも
のを実施例2とした。比較例2についで、実施例1と同
様の方法でアミノ基を導入し、次番こジオキサン中で無
水フI\り酸と室温で6時間反応させてカルボキシル基
を導入したものを比較例6として使用した。平均細孔直
径が1300^の多孔性ガラスに実施例1と同様の方法
で41.7μmad/ fのスルホン酸基を導入したも
のを実施例3(n=15001、細孔直径が0.8D〜
1.2Dにある細孔容積の割合90%、細孔容積1−0
5cc/り9粒径0.2−〜0.5111)とした。平
均細孔直径が1400Xの多孔性ガラス(n=1400
に、細孔直径が0.8D〜1.2Dにある細孔容積の割
合88%、細孔容90.94cc/f 、粒径0.2 
wm 〜0.5 m )に実施例1と同様の)5法で2
6.8μmail /fのスルホン酸基を導入したもの
を実施例4とした。また、平均細孔直径が560にの多
孔性ガラスに実施例1と同様の方法でスルホン酸基を導
入したもの(D、、560A、細孔直径が0.8D〜1
.2Dにある細孔容積の割合91%、細孔容積0.76
cc/f、粒径0.21m11〜0.51121+、ス
ルホン酸基濃度71.5μmog/? )を比較例4と
して使用し心実施例1〜4と比較例1〜4についで、各
22をポリプロピレン製のカフム(両端に180メツシ
ユのポリエステル製のフィルター付)に充填し、ウサギ
血漿20購1を57℃で3時間循環した。循環前後の総
蛋白質濃度をビウレット法で、コレステロール濃度をオ
ルト−フタルアルデヒド法でそれぞれ定量し除去率を計
算した。(除去率(%)−(1−循環後濃度/循環前濃
度)X100)、コレスプロールは血液中に単独で存在
することはほとんど無く、大部分が低密度リボ蛋白質と
結合して存在しでいる。従ってコレステロールの除去率
と低密度リポ蛋白質の除去率は実質上等しいと考えられ
るので、コレステロールの濃度を分析した。
Porous glass with an average pore diameter of 1060λ (n=1060
^, The proportion of pore volume with a pore diameter of 0.8D to 1.2D is 81%, the pore volume is 0.92cc/p, the particle size is 0.2cm to
0.5m) was designated as Comparative Example 2, and Example 2 was obtained by introducing 54.5 μmol/f of sulfonic acid groups into this in the same manner as in Example 1. Following Comparative Example 2, an amino group was introduced in the same manner as in Example 1, and then a carboxyl group was introduced by reacting with fluoric anhydride in dioxane at room temperature for 6 hours. used as. Example 3 (n = 15001, pore diameter 0.8D ~
1.90% of pore volume in 2D, pore volume 1-0
The particle size was 0.2-0.5111) at 5 cc/liter. Porous glass with an average pore diameter of 1400X (n=1400
The proportion of pore volume with a pore diameter of 0.8D to 1.2D is 88%, the pore volume is 90.94cc/f, and the particle size is 0.2D.
wm ~ 0.5 m) by the same method as in Example 1).
Example 4 was prepared by introducing a sulfonic acid group of 6.8 μmail/f. In addition, a porous glass with an average pore diameter of 560 and a sulfonic acid group introduced in the same manner as in Example 1 (D, 560A, a pore diameter of 0.8D to 1
.. Percentage of pore volume in 2D: 91%, pore volume: 0.76
cc/f, particle size 0.21ml~0.51121+, sulfonic acid group concentration 71.5μmog/? ) was used as Comparative Example 4. Following Examples 1 to 4 and Comparative Examples 1 to 4, 22 of each were filled into a polypropylene cuff (with a 180-mesh polyester filter on both ends), and 20 rabbit plasma were purchased. 1 was circulated at 57°C for 3 hours. The total protein concentration before and after circulation was determined by the biuret method, and the cholesterol concentration was determined by the ortho-phthalaldehyde method, and the removal rate was calculated. (Removal rate (%) - (1 - post-circulation concentration / pre-circulation concentration) x 100), cholesprol rarely exists alone in the blood, and most of it exists bound to low-density riboproteins. There is. Therefore, since the removal rate of cholesterol and the removal rate of low-density lipoprotein are considered to be substantially equal, the concentration of cholesterol was analyzed.

表1に示すように実施例の吸着剤による総蛋白の減少は
少なく、コレステロールは70%前後がない比較例1〜
3では、コレステロール除去率が低かった。また、平均
細孔直径が700Aより小さい比較例4では、コレステ
が−ルの除去率は太きいが、総蛋白質の除去率も大きく
なり選択性の低いものであった。
As shown in Table 1, the decrease in total protein due to the adsorbent of the example is small, and the cholesterol content is around 70%.
3, the cholesterol removal rate was low. In Comparative Example 4, in which the average pore diameter was smaller than 700 A, the removal rate of cholesterol was high, but the removal rate of total protein was also high, resulting in low selectivity.

第     1     表 特許出願人 株式会社り ラ し 代理人弁理士本多 堅Chapter 1 Table Patent applicant Rishi Co., Ltd. Representative Patent Attorney Ken Honda

Claims (1)

【特許請求の範囲】 1、表面にスルホン酸基を有し、かつ平均細孔直径が7
00A〜200OAの範囲内にある多孔体であることを
特徴とする低密度IJ 、tF蛋白質吸着剤。 2、平均細孔直径が900A〜1/+OOAの範囲内に
ある特許請求の範囲第1項記載の低密度リポ蛋白質吸着
剤。 5、多孔体の細孔容積が0.3 cc/f 以上、2.
0 cc/1? 以下である特許請求の範囲第1項、第
2項のいずれかに記載の低密度リポ蛋白質吸着剤。 4、多孔体の粒子直径が0.1.〜5端の範囲内にある
特許請求の範囲第1項〜第3項のいずれかに記載の低密
度リポ蛋白質吸着剤。 5、多孔体が、平均細孔直径をDとするとき細孔直径が
0,8D〜1.2Dの範囲内にある細孔の容積の割合が
全細孔容積の80%以上を占める多。 孔体である特許請求の範囲第1項〜第4項のいず口かに
記載の低密度リポ蛋白質吸着剤。
[Claims] 1. Has a sulfonic acid group on the surface and has an average pore diameter of 7.
A low-density IJ, tF protein adsorbent characterized by being a porous material having a porosity within the range of 00A to 200OA. 2. The low-density lipoprotein adsorbent according to claim 1, having an average pore diameter within the range of 900A to 1/+OOA. 5. The pore volume of the porous body is 0.3 cc/f or more; 2.
0 cc/1? A low-density lipoprotein adsorbent according to any one of claims 1 and 2 below. 4. The particle diameter of the porous body is 0.1. The low-density lipoprotein adsorbent according to any one of claims 1 to 3, which falls within the range of . 5. In the porous body, the proportion of the volume of pores having a pore diameter in the range of 0.8D to 1.2D, where D is the average pore diameter, accounts for 80% or more of the total pore volume. The low-density lipoprotein adsorbent according to any one of claims 1 to 4, which is a porous body.
JP56126443A 1981-08-11 1981-08-11 Low density lipoprotein adsorbent Pending JPS5827559A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56126443A JPS5827559A (en) 1981-08-11 1981-08-11 Low density lipoprotein adsorbent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56126443A JPS5827559A (en) 1981-08-11 1981-08-11 Low density lipoprotein adsorbent

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP57043619A Division JPS5826819A (en) 1982-01-05 1982-03-17 Porous glass adsorbent for low-density lipoprotein particles

Publications (1)

Publication Number Publication Date
JPS5827559A true JPS5827559A (en) 1983-02-18

Family

ID=14935330

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56126443A Pending JPS5827559A (en) 1981-08-11 1981-08-11 Low density lipoprotein adsorbent

Country Status (1)

Country Link
JP (1) JPS5827559A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59200655A (en) * 1983-04-30 1984-11-14 旭化成株式会社 Blood purifying and adsorbing material
JPS60114340A (en) * 1983-11-25 1985-06-20 Asahi Chem Ind Co Ltd Adsorbent for adsorption of low specific gravity lipoprotein
JPS60242863A (en) * 1984-05-18 1985-12-02 旭化成株式会社 Porous adsorbing material for adosorbing low specific gravity lipoprotein
JPS60246764A (en) * 1984-05-22 1985-12-06 旭化成株式会社 Method and apparatus for adsorbing low specific gravity lipoprotein
US4826679A (en) * 1986-05-23 1989-05-02 Universite De Montreal Composition and methods for alleviating cystic fibrosis
JPH02257964A (en) * 1988-11-09 1990-10-18 Chembiomed Ltd Improved affinity carrier for blood irrigation
US6582386B2 (en) 2001-03-06 2003-06-24 Baxter International Inc. Multi-purpose, automated blood and fluid processing systems and methods
US6706008B2 (en) 2001-03-06 2004-03-16 Baxter International Inc. Automated system and method for withdrawing compounds from blood
US6884228B2 (en) 2001-03-06 2005-04-26 Baxter International Inc. Automated system adaptable for use with different fluid circuits

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59200655A (en) * 1983-04-30 1984-11-14 旭化成株式会社 Blood purifying and adsorbing material
JPH0429396B2 (en) * 1983-04-30 1992-05-18
JPS60114340A (en) * 1983-11-25 1985-06-20 Asahi Chem Ind Co Ltd Adsorbent for adsorption of low specific gravity lipoprotein
JPH043988B2 (en) * 1983-11-25 1992-01-24
JPS60242863A (en) * 1984-05-18 1985-12-02 旭化成株式会社 Porous adsorbing material for adosorbing low specific gravity lipoprotein
JPS6359344B2 (en) * 1984-05-18 1988-11-18
JPS60246764A (en) * 1984-05-22 1985-12-06 旭化成株式会社 Method and apparatus for adsorbing low specific gravity lipoprotein
US4826679A (en) * 1986-05-23 1989-05-02 Universite De Montreal Composition and methods for alleviating cystic fibrosis
JPH02257964A (en) * 1988-11-09 1990-10-18 Chembiomed Ltd Improved affinity carrier for blood irrigation
US6582386B2 (en) 2001-03-06 2003-06-24 Baxter International Inc. Multi-purpose, automated blood and fluid processing systems and methods
US6706008B2 (en) 2001-03-06 2004-03-16 Baxter International Inc. Automated system and method for withdrawing compounds from blood
US6884228B2 (en) 2001-03-06 2005-04-26 Baxter International Inc. Automated system adaptable for use with different fluid circuits

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