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JPH04187206A - Leucocyte separator and production of leucocyte separating material - Google Patents

Leucocyte separator and production of leucocyte separating material

Info

Publication number
JPH04187206A
JPH04187206A JP31479490A JP31479490A JPH04187206A JP H04187206 A JPH04187206 A JP H04187206A JP 31479490 A JP31479490 A JP 31479490A JP 31479490 A JP31479490 A JP 31479490A JP H04187206 A JPH04187206 A JP H04187206A
Authority
JP
Japan
Prior art keywords
blood
ethylene glycol
leukocyte
leucocyte
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.)
Pending
Application number
JP31479490A
Other languages
Japanese (ja)
Inventor
Hidehiko Sakurai
桜井 秀彦
Akira Yagi
晃 八木
Hideyuki Ohashi
大橋 英之
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.)
Toyobo Co Ltd
Original Assignee
Toyobo 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 Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP31479490A priority Critical patent/JPH04187206A/en
Publication of JPH04187206A publication Critical patent/JPH04187206A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)
  • Filtering Materials (AREA)

Abstract

PURPOSE:To obtain the device which efficiently and safely removes leucocytes and allows the permeation of platelets by constituting a part of the leucocyte separating material and/or the inside of a housing with a polymer of ethylene glycol. CONSTITUTION:This device is constituted of the leucocyte separating material consisting of an extremely fine non-woven fabric and a porous membrane, etc., and the housing. The polymer of the ethylene glycol is introduced into at least a part of the leucocyte separating material in contact with the blood, etc., and/or the inside of the housing. This introduction is executed by a method of first dissolving the diacrylate of the polymer of the ethylene glycol into a solvent, such as alcohol, immersing the separating material, etc., therein to deposit this material, etc., then evaporating the solvent. The material is then irradiated with radiations to polymerize the diacrylate of the ethylene glycol polymer on the surface by which the material is coated with this polymer. The unpolymerized matter is washed and extracted in the solvent and is dried. Only the leucocytes are efficiently and safely separated by using this material.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、血液もしくは血液の成分から白血球を除去す
る装置、さらに詳しくは、血液もしくは血液の成分から
血小板は透過し、白血球のみを効率的かつ安全に選択分
離除去するための白血球分離材料及び装置に関する。
Detailed Description of the Invention (Industrial Application Field) The present invention is an apparatus for removing leukocytes from blood or blood components. The present invention also relates to leukocyte separation materials and devices for safe selective separation and removal.

(従来の技術) 近年の輸血に対する考え方は、従来の全血輸血に代わっ
て、患者が必要とする成分のみを輸血する成分輸血が主
として用いられる。例えば出血傾向のある患者や何等か
の理由で血液中の血小板数が減少した患者には、止血効
果の高い血小板製剤を繰り返し輸血する。しかしながら
、血小板製剤は遠心分離法によって作製されるため、血
小板と白血球の密度差が小さいことから、血小板製剤に
は大量の白血球が混入している。本来生体にとって有用
な白血球も、輸血においてはを害物質となる。すなわち
繰り返し輸血された他人の白血球により受血者体内に抗
白血球抗体が産生され、この抗白血球抗体によって発熱
二悪寒、頭痛、吐き気、アレルギー反応などの輸血副作
用が発生したり、輸血された血小板の生存率が低下する
。また、輸血されたリンパ球が受血者の体内組織を異物
と註。
(Prior Art) In recent years, the approach to blood transfusion has been to replace the conventional whole blood transfusion with component transfusion, in which only the components required by the patient are transfused. For example, patients who tend to bleed or who have a decreased number of platelets in their blood for some reason are repeatedly transfused with a platelet preparation that has a high hemostasis effect. However, since platelet preparations are produced by centrifugation, the difference in density between platelets and white blood cells is small, so platelet preparations contain a large amount of leukocytes. White blood cells, which are originally useful to living organisms, become harmful substances in blood transfusions. In other words, anti-leukocyte antibodies are produced in the recipient's body due to repeated transfusions of other people's leukocytes, and these anti-leukocyte antibodies can cause transfusion side effects such as fever, chills, headache, nausea, and allergic reactions, and may cause the blood platelets that have been transfused to Survival rate decreases. Also, the transfused lymphocytes treat the recipient's internal tissues as foreign substances.

識し、攻撃するG V HDという重要な拒絶反応を引
き起こすことがある。以上のような理由から、血小板輸
血に関して、混入白血球の除去の必要性が強く唱えられ
ている。
This can cause an important rejection reaction called G V HD, which recognizes and attacks G V HD. For the reasons mentioned above, the necessity of removing contaminated leukocytes with respect to platelet transfusion is strongly advocated.

また、リウマチ等の自己免疫疾患患者の体液からリンパ
球を除去することにより臨床症状が改善することが報告
されている。(例えば、船越ら、慢性関節リウマチ患者
への免疫療法としての胸管ドレナージの試み、人工臓器
 17(2) 417(19E18))体液中からリン
パ球を除去する方法には、血液或はリンパ液を採取し、
その中に含まれるリンパ球を除去する方法があるが、操
作の手軽さや、連続性の観点から前者の方が好ましい。
Furthermore, it has been reported that clinical symptoms are improved by removing lymphocytes from the body fluids of patients with autoimmune diseases such as rheumatism. (For example, Funakoshi et al., Trial of thoracic duct drainage as immunotherapy for rheumatoid arthritis patients, Artificial Organs 17(2) 417(19E18)) Methods for removing lymphocytes from body fluids include the use of blood or lymph fluid. Collect,
Although there is a method for removing the lymphocytes contained therein, the former is preferable from the viewpoint of ease of operation and continuity.

しかし、血液からの白血球除去においては、共存する血
小板も同時に除去してしまう恐れがある。そのため血小
板を補足しない血液からの白血球除去方法の開発が強く
望まれている。
However, when removing leukocytes from blood, there is a risk that coexisting platelets may also be removed at the same time. Therefore, there is a strong desire to develop a method for removing leukocytes from blood that does not supplement platelets.

血液やその成分もしくは血小板製剤より白血球を除去す
る方法には、遠心分離による方法があるが、これは装置
が高価であること、赤血球、白血球の除去率、血小板の
回収率共に低いこと、操作が複雑であり、献血時や輸血
時にオンライン処理ができないこと等の問題がある。
Centrifugation is a method for removing white blood cells from blood, its components, or platelet preparations, but this method requires expensive equipment, low red blood cell and white blood cell removal rates, and low platelet recovery rates, and is difficult to operate. It is complicated, and there are problems such as the inability to perform online processing at the time of blood donation or transfusion.

一方近年極細繊維不織布フイルターを用いた白血球除去
装置が開発され、赤血球製剤中の白血球除去に使用され
ている。(例えば特開昭6l−276564)これらの
白血球除去装置は、赤血球製剤中の白血球を効率よく除
去でき、装置も小型で操作も容易であるが、血小板も同
時に分離除去してしまうため、血小板製剤中の白血球を
除去する用途には使用できない。これらの装置を末梢血
体外循環に使用しリウマチ等の自己免疫疾患の治療に用
いた例も見られるが(例えば平良ら、白血球除去フィル
ターによるIeucocytapheresis 1)
fi床効果と安全性人工臓器 16(2) (1987
) )血小板が大部分補足されてしまう問題点があった
On the other hand, in recent years, a leukocyte removal device using a microfiber nonwoven filter has been developed and is used to remove leukocytes from red blood cell preparations. (For example, Japanese Patent Application Laid-Open No. 61-276564) These leukocyte removal devices can efficiently remove leukocytes from red blood cell preparations, and are small and easy to operate. However, since platelets are also separated and removed at the same time, It cannot be used to remove white blood cells inside. There are also examples of using these devices for peripheral blood extracorporeal circulation to treat autoimmune diseases such as rheumatism (e.g., Taira et al., Ieucocytapheresis 1 using a leukocyte removal filter).
FI bed effect and safety of artificial organs 16(2) (1987
)) There was a problem that most of the platelets were captured.

そこで、これらの極細繊維不織布フィルターの表面に親
水性物質のコーティングを施し、血小板の透過性を高め
ようとする試みが見られている。
Therefore, attempts have been made to coat the surface of these ultrafine fiber nonwoven fabric filters with a hydrophilic substance to increase the permeability of platelets.

(例えば官本ら;血小板輸血用白血球除去フィルターの
開発、日本輸血学会誌、35 (3) 、 370−3
74(1!IE19)、表等ら:被覆化フィルターによ
る白血球除去療法−RA患者にお&−する免疫学的検討
−人工臓器 18(3) (1989) )これによる
と、コーティングによって血小板の透過率が上昇し、か
つ99%以上の白血球が除去されている。しかしながら
、この種のコーティング剤には親水基として一011基
を導入しているため補体が活性化されてしまう。
(For example, Kanmoto et al.; Development of leukocyte removal filter for platelet transfusion, Journal of the Japanese Society of Blood Transfusion, 35 (3), 370-3
74 (1! IE19), Table et al.: Leukocyte depletion therapy using coated filters - Immunological studies for RA patients - Artificial organs 18 (3) (1989)) According to this, the coating reduces the permeation of platelets. rate has increased and more than 99% of white blood cells have been removed. However, since this type of coating agent has 1011 groups introduced as hydrophilic groups, complement is activated.

また、コーテイング材や重合時の触媒の安定性も安全性
の上で重要な因子であるが、従来までのコーティングを
施した白血球除去フィルターでは本発明者らのこれまで
の検討では、溶出物の量が多く、現在の厚生省透析型人
工腎臓承認基準の溶出物試験の項に合格する白血球除去
フィルターはなく、これらのフィルターの安全性は充分
とはいえない。
In addition, the stability of coating materials and catalysts during polymerization is also an important factor in terms of safety, but with conventional coated leukocyte removal filters, the present inventors have found that eluate There are no leukocyte removal filters that pass the eluate test section of the current Ministry of Health and Welfare's approval standards for dialysis-type artificial kidneys, and the safety of these filters cannot be said to be sufficient.

(発明が解決しようとする課題) 従来までのコーティングを施した不織布フィルターによ
る白血球除去フィルターでは、コーテイング材による血
液中の補体成分の活性化や、コーテイング材の処理液中
への溶出が問題となっていた。
(Problems to be Solved by the Invention) Conventional white blood cell removal filters using coated nonwoven fabric filters have problems such as activation of complement components in blood by the coating material and elution of the coating material into the processing solution. It had become.

本発明は血液もしくは血液成分や血小板製剤中から効率
的にかつ安全に白血球を除去し、かつ血小板を透過する
だめの装置および装置の製造方法を提供することを目的
とする。
An object of the present invention is to provide a device and a method for manufacturing the device that can efficiently and safely remove leukocytes from blood or blood components or platelet preparations, and that can permeate platelets.

(課題を解決するための手段) すなわち、本発明は(1)  ハうジング内に白血球分
離材料を収納さ・lてなる血液もしくは血液の成分と接
触し、該血液もしくは血液成分中から白血球を除去する
装置において、血液もしくは血液成分と接触する白血球
分離材料及び/又はハウジング内部の少なくとも1部分
がエチレングリコールの多量体を有する白血球分離装置
及び (2)  エチレングリコールの多量体のジアクリレー
トを白血球除去フィルター素材に担持させた後、放射線
を照射させることにより表面にエチレングリコールの多
量体を重合させる白血球分離材料の製造方法である。
(Means for Solving the Problems) That is, the present invention provides (1) a method in which a leukocyte separation material is housed in a housing and comes into contact with blood or blood components, and leukocytes are removed from the blood or blood components. (2) a leukocyte separation device in which at least a portion of the leukocyte separation material and/or the interior of the housing that contacts blood or blood components has an ethylene glycol polymer; This is a method for producing a leukocyte separation material in which a leukocyte separation material is supported on a filter material and then irradiated with radiation to polymerize an ethylene glycol polymer on the surface.

従来までの血小板製剤処理用白血球除去フィルターのコ
ーティング材料としては、ヒドロキシエチルメタクリレ
ート(以下II E M Aと略す)が、おもに用いら
れてきた。これは011基を導入することにより、血小
板と素材間の相互作用を弱め、血小板の透過率を向上さ
せることを目標としている。しかしながら血小板の透過
率を向上させるという所期の目標は達せられたが、その
ために凝固系や免疫系を司る血漿中の補体というタンパ
ク質が活性化されるという問題点が生じた。また、コー
ティング材料が処理液中・に溶出する危険性があること
も判明した。そこで、本発明者らは、種々の物質のコー
ティングを施した不織布フィルターを作製し、血液や血
小板製剤の処理を行い、コーティング材料と白血球除去
率、血小板透過率、補体活性化との関係について鋭意検
討を行った。また、溶出物のないコーティングについて
種々の触媒や、方法を鋭意検討した。その結果、材料表
面にエチレングリコールの多量体を付与することにより
血小板透過性にすくれ、補体を活性化しないことを見い
だした。また、エチレングリコールの多量体のジアクリ
レートを白血球除去フィルター素材に担持させた後、表
面に放射線を照射することにより表面にエチレングリコ
ールの多量体を重合させることによりコーテイング材に
安定性を賦与可能であることを見いだし本発明に至った
。以下本発明について詳細に説明する。
Conventionally, hydroxyethyl methacrylate (hereinafter abbreviated as IIEMA) has been mainly used as a coating material for leukocyte removal filters for treating platelet preparations. This aims to weaken the interaction between platelets and materials and improve the permeability of platelets by introducing the 011 group. However, although the initial goal of improving platelet permeability was achieved, a problem arose in that it activated a protein called complement in plasma, which controls the coagulation and immune systems. It was also found that there is a risk that the coating material may be leached into the processing solution. Therefore, the present inventors fabricated nonwoven fabric filters coated with various substances, processed blood and platelet products, and investigated the relationship between the coating material and leukocyte removal rate, platelet permeability, and complement activation. We conducted a thorough study. In addition, various catalysts and methods for coating without eluents were intensively investigated. As a result, they found that adding a multimer of ethylene glycol to the surface of the material reduces platelet permeability and does not activate complement. In addition, stability can be imparted to the coating material by supporting the leukocyte removal filter material with ethylene glycol polymer diacrylate and then irradiating the surface with radiation to polymerize the ethylene glycol polymer on the surface. This discovery led to the present invention. The present invention will be explained in detail below.

本発明に用いる白血球除去装置は白血球分離材料及びハ
ウジングを主たる構成要素とし、該分離材血液もしくは
血液の成分と接触して白血球を除去するものであれば材
料や構造は特に限定されるものではないが、例としては
極細繊維不織布や多孔質膜、ガラスピーズ、スポンジ構
造状物が挙げられる。
The leukocyte removal device used in the present invention has a leukocyte separation material and a housing as its main components, and the material and structure are not particularly limited as long as the separation material can remove leukocytes by contacting blood or blood components. However, examples include microfiber nonwoven fabrics, porous membranes, glass beads, and sponge structures.

本発明においては血液もしくは血液の成分と接触する装
置表面の少なくとも1部分にエチレングリコールの多量
体を含むことを特長とする。即ち本装置は通常、材料と
それを設置するハつジングとからなり、また白血球分離
材料も処理液中に含まれる微小塊を除去するプレフィル
タ一部と白血球除去フィルタ一部に分割することができ
、ハウジングの内側やプレフィルタ−も血液もしくは血
液成分と接触するので、白血球除去フィルターだけでな
くこれらの部分にエチレングリゴールの多量体を導入す
ることが必要になる。し・がし最も好ましいのは白血球
除去フィルターにエチレングリコールの多量体を導入す
ることである。
The present invention is characterized in that at least a portion of the surface of the device that comes into contact with blood or blood components contains an ethylene glycol polymer. That is, this device usually consists of a material and a housing for installing the same, and the leukocyte separation material can also be divided into a pre-filter for removing minute particles contained in the processing liquid and a leukocyte-removing filter. Since the inside of the housing and the prefilter also come into contact with blood or blood components, it is necessary to introduce a polymer of ethylene glycol into these parts as well as the leukocyte removal filter. Most preferably, a multimer of ethylene glycol is introduced into the leukocyte removal filter.

本発明におけるエチレンゾ・リコールの多量体とは二量
体以上のエチレングリゴールを指す。本発明におけるエ
チレングリコール多量体の分子量に特に規定はないが、
安定性の面から、あまり大きすぎない方がよく、好まし
くは分子量1500以下のポリエチしくグリコールが、
より好ましくは分子量600以下のポリエチレングリコ
ールを用いることがよい。
In the present invention, the term "ethylenezo glycol multimer" refers to ethylene glycol in the form of a dimer or more. Although there is no particular restriction on the molecular weight of the ethylene glycol polymer in the present invention,
From the viewpoint of stability, it is better not to have too large a size, and preferably a polyethylene glycol with a molecular weight of 1500 or less,
More preferably, polyethylene glycol having a molecular weight of 600 or less is used.

本発明の白血球除去ライルターへのエチレングリコール
多量体の導入方法は、グラフト重合や、素材中への混合
q等、種々考えられるが、触媒を使用しないことや溶出
物が少ないことからエチレングリコ・−ル多量体のジア
クリレートを放射線重合により素材表面にコーティング
することが望ましい。コーティングの方法は一般的に知
られており、特に限定するもので、はないが、例えば以
下の様な方法が知られている。エチレングリコール多量
体のジアクリレートを溶媒(アルコール、水等)に溶か
し、フィルター素材を該溶液に浸漬し、該エチレングリ
コール多量体のジアクリレートを該素材に担持させた後
、該溶媒を蒸発させる。その後、表面のエチレングリコ
ール多量体のジアクリレートを重合させるに充分な放射
線を照射する。未重合のモノマーをアルコールや水等の
溶媒中で洗浄、抽出し、乾燥する。
Various methods of introducing the ethylene glycol polymer into the leukocyte-removing Lylter of the present invention are possible, such as graft polymerization and mixing into the material, but ethylene glycol- It is desirable to coat the surface of the material with a multimeric diacrylate by radiation polymerization. Coating methods are generally known and are not particularly limited, but for example, the following methods are known. The diacrylate of the ethylene glycol polymer is dissolved in a solvent (alcohol, water, etc.), the filter material is immersed in the solution, the diacrylate of the ethylene glycol polymer is supported on the material, and then the solvent is evaporated. Thereafter, radiation sufficient to polymerize the diacrylate of the ethylene glycol polymer on the surface is irradiated. The unpolymerized monomer is washed in a solvent such as alcohol or water, extracted, and dried.

ハウジングは入口と出口を有し、円筒状カラム、盆状体
等の形状を有し、材料としてはポリエステル、ポリカー
ボネート等のプラスチックが用いられ不透明であっても
よいが内部の濾過状態が観察できる透明プラスチックが
好ましい。
The housing has an inlet and an outlet, and has the shape of a cylindrical column, tray, etc., and is made of plastic such as polyester or polycarbonate, and may be opaque, but it is transparent so that the internal filtration state can be observed. Plastic is preferred.

−l O− 以下実施例により本発明の効果並びにより詳細な説明を
加える。
-l O- The effects of the present invention and more detailed explanation will be added below using Examples.

(実施例) 本発明における実施例および比較例では、白血球分離材
料の素材としてメルトブロー法により得られたポリエチ
レンテレフタレートの極細繊維不織布(糸径1.5μm
)を用いた。
(Example) In the Examples and Comparative Examples of the present invention, an ultrafine fiber nonwoven fabric (thread diameter 1.5 μm) of polyethylene terephthalate obtained by melt blowing was used as a material for leukocyte separation material.
) was used.

また、白血球の除去率、血小板の透過率はACD添加新
鮮牛血液より遠心分離して作成した多血小板血漿(以下
PPPと略す)を使用し測定した。白血球数、血小板数
はコールタ−カウンターを用い常法により測定し、フィ
ルターを通過した前後の白血球数、血小板数より白血球
除去率、血小板透過率を計算した。  ′ 生体適合性の評価は、新鮮人血液に抗凝固剤としてAC
D液を添加したものを用い、補体成分の一つであるC3
の活性化体であるC3mの濃度をフィルター通過前後で
測定することで行った。C,la濃度は、ラジオイムノ
アッセイ法により測定した。
In addition, the leukocyte removal rate and platelet permeability were measured using platelet-rich plasma (hereinafter abbreviated as PPP) prepared by centrifuging fresh bovine blood supplemented with ACD. The number of white blood cells and platelets were measured by a conventional method using a Coulter counter, and the leukocyte removal rate and platelet permeability were calculated from the number of white blood cells and platelets before and after passing through the filter. 'Biocompatibility evaluation was performed using AC as an anticoagulant in fresh human blood.
C3, which is one of the complement components, is used to add D solution.
The concentration of C3m, which is an activated form of C3m, was measured before and after passing through the filter. C,la concentration was measured by radioimmunoassay method.

溶出物試験は日本薬局方輸液用プラスチック容器試験法
の溶出物試験法に準じ、試料1gを100戚の純水中で
121°C11時間の溶出を行い、得られた溶出液を分
析することによって行った。試験項目は、性状、あわだ
ち、pH1紫外吸収スペクトルである。また、溶出液の
全有機炭素含有量も併せて測定した。
The eluate test was carried out in accordance with the eluate test method of the Japanese Pharmacopoeia Test Method for Plastic Containers for Infusions, in which 1 g of the sample was eluted in 100% pure water at 121°C for 11 hours, and the resulting eluate was analyzed. went. Test items are properties, foam, and pH 1 ultraviolet absorption spectrum. In addition, the total organic carbon content of the eluate was also measured.

実施例1 ポリエチレングリコール(分子量400)のジアクリレ
ートの2,5%メタノール溶液を作製した。
Example 1 A 2.5% methanol solution of diacrylate of polyethylene glycol (molecular weight 400) was prepared.

メルトブロー法によって作製した糸径1.5μ耐の極細
繊維不織布を、この?8液に1分間浸漬後、真空乾燥機
にて、80°C112時間乾燥を行った。乾燥した不織
布に10Mradの電子線を照射し、重合反応を行った
。未反応子ツマ−を除去するため、高温純水で洗浄を行
った後乾燥機で80°C112時間乾燥した。
This ultra-fine fiber non-woven fabric with a thread diameter of 1.5μ produced by the melt-blowing method is After being immersed in Liquid 8 for 1 minute, it was dried in a vacuum dryer at 80°C for 112 hours. The dried nonwoven fabric was irradiated with an electron beam of 10 Mrad to perform a polymerization reaction. In order to remove unreacted particles, the product was washed with high-temperature pure water and then dried in a dryer at 80°C for 112 hours.

コーティング前後の重量変化により、不織布の30%の
重量のポリエチレングリコールがコーティングされてい
た。
The weight change before and after coating showed that 30% of the weight of the nonwoven fabric was coated with polyethylene glycol.

このコーティングされた不織布を0.7g計りとわ、面
積10c+iのミニモジュールに組み込み、牛血液実験
に供した。処理速度5mfi/minで100mj!の
PRPを処理したところ、白血球の除去率は99.8%
、血小板の透過率は98%であった。また、同じように
組み立てたモジュールにヒト血液を流し、補体活性を検
討したところ、C3aの値はフィルター通過前240n
g/蔵、フィルター通過後320ng/mff1であり
、通過前後の値に有意差はなかった。
This coated nonwoven fabric was weighed out in an amount of 0.7 g and was incorporated into a mini module having an area of 10 c+i, and was used in a bovine blood experiment. 100mj at a processing speed of 5mfi/min! When treated with PRP, the leukocyte removal rate was 99.8%.
, the platelet permeability was 98%. In addition, when human blood was poured into a module assembled in the same way and complement activity was examined, the C3a value was 240n before passing through the filter.
g/cell and 320 ng/mff1 after passing through the filter, and there was no significant difference between the values before and after passing.

次に純水100gにこの不織布1.0 gを加え、オー
トクレーブ中で121°C11時間の溶出を行い、得ら
れた溶出液を用いて、溶出物試験を行った。性状、紫外
線吸光度、泡立ち試験、pH変化量は全て基準以下であ
った。また、溶出液の全有機炭素含有量量は、10pp
mであった。
Next, 1.0 g of this nonwoven fabric was added to 100 g of pure water, and elution was performed in an autoclave at 121° C. for 11 hours. Using the obtained eluate, an eluate test was conducted. The properties, ultraviolet absorbance, foaming test, and pH change were all below standards. In addition, the total organic carbon content of the eluate was 10 pp
It was m.

実施例2 ポリエチレングリコール(分子量200)のジアクリレ
ートの1.0%メタノール溶液を作成した。
Example 2 A 1.0% methanol solution of diacrylate of polyethylene glycol (molecular weight 200) was prepared.

実施例1と同様の極細繊維不織布を、この溶液に1分間
浸漬後、真空乾燥機にて、80’C,12時間乾燥を行
った。乾燥した不織布に5Mradのγ線を照射し、重
合反応を行った。実施例1と同様に未反応モノマーを除
去し、乾燥した。
The same microfiber nonwoven fabric as in Example 1 was immersed in this solution for 1 minute, and then dried in a vacuum dryer at 80'C for 12 hours. The dried nonwoven fabric was irradiated with 5 Mrad of gamma rays to perform a polymerization reaction. Unreacted monomers were removed and dried in the same manner as in Example 1.

コーティング前後の重量変化より、不織布の12%の重
量のポリエチレングリコールがコーティングされていた
From the weight change before and after coating, it was found that 12% of the weight of the nonwoven fabric was coated with polyethylene glycol.

実施例1と同様なミニモジュールに組み込み、牛血液実
験に供したところ、白血球の除去率は99.5%血小板
の透過率は99%であった。また、補体活性を検討した
ところ、C3aの値はフィルター通過前240ny、/
ml、フィルター通過後310ng/dであり、通過前
後の値に有意差はなかった。
When it was incorporated into the same mini module as in Example 1 and subjected to a bovine blood experiment, the leukocyte removal rate was 99.5%, and the platelet permeability was 99%. In addition, when complement activity was examined, the value of C3a was 240 ny before passing through the filter, /
ml and 310 ng/d after passing through the filter, and there was no significant difference between the values before and after passing.

溶出物試験では全て基準以下であった。また、溶出液の
全有機炭素含有量量は、8 ppmであった。
All eluate tests were below standards. Further, the total organic carbon content of the eluate was 8 ppm.

比較例1 実施例1と同し極細繊維不織布をコーティング処理を行
わないまま用いた。
Comparative Example 1 The same ultrafine fiber nonwoven fabric as in Example 1 was used without being coated.

実施例1と同様のモジュールを用い、同じ条件でPPP
を流したところ、白血球の除去率は99.5%であった
が、血小板の透過率は、30%であった。
PPP using the same module as in Example 1 and under the same conditions.
The leukocyte removal rate was 99.5%, but the platelet permeability was 30%.

また、処理量が50戒越えると目詰まりが発生し、フィ
ルター通過前後の圧力損失が増加し、100mfi処理
時には150mm1gとなった。
In addition, when the throughput exceeds 50 precepts, clogging occurs, and the pressure loss before and after passing through the filter increases, and the amount was 150 mm/g at the time of 100 mfi treatment.

ヒト血液実験による補体の活性化試験では、C3a値は
フィルター通過前で240ng/if、フィルター通過
後で300ng/ mIlであり、フィルター通過前後
でC3a値に有為な違いを認めなかった。
In a human blood complement activation test, the C3a value was 240 ng/if before passing through the filter and 300 ng/ml after passing through the filter, and no significant difference was observed in the C3a value before and after passing through the filter.

121°Cの溶出物試験では、全ての項目で基準値以下
だった。溶出液の全有機炭素含有量量は、5 ppmで
あった。
In the eluate test at 121°C, all items were below standard values. The total organic carbon content of the eluate was 5 ppm.

比較例2 実施例1と同じ極細繊維不織布に2−ヒドロキシエチル
アクリレートを実施例1と同様な方法でコーティングし
た。コーテイング量は不織布の重量比25%であった。
Comparative Example 2 The same ultrafine fiber nonwoven fabric as in Example 1 was coated with 2-hydroxyethyl acrylate in the same manner as in Example 1. The coating amount was 25% by weight of the nonwoven fabric.

′ 実施例1と同様のモジュール、条件で牛血液実験を行っ
たところ白血球の除去率99,8%、血小板の透過率9
0%であり、フィルターの目詰まりもなく安定した操作
が可能であった。
' When a bovine blood experiment was conducted using the same module and conditions as in Example 1, the leukocyte removal rate was 99.8% and the platelet penetration rate was 9.
0%, and stable operation was possible without clogging of the filter.

ヒト血液実験による補体活性化試験ではqcaa値はフ
ィルター通過前で240ng/alt、フィルター通過
後で1300ng/IdlでCaa値が通過前後で有意
に増加していた。これは、2−ヒドロキシエチルアクリ
レートが0■基を持つためと考えられた。
In a complement activation test based on human blood experiments, the QCaa value was 240 ng/alt before passing through the filter, and 1300 ng/Idl after passing through the filter, and the Caa value significantly increased before and after passing through the filter. This was considered to be because 2-hydroxyethyl acrylate has 0 groups.

121℃の溶出物試験では、紫外線吸光度が0.350
で基準値以上となった。その他の項目は基準値以下であ
ったが、溶出液の全有機炭素含有量は48pp111で
あった。実施例1に比べて紫外吸光度、全有機炭素含有
量が多いのは、2−ヒドロキシエチルアクリレートのア
クリレート基が1つであり、実施例1のPI!G400
のジアクリレートと比べて結合力が弱いためと考えられ
た。
In the eluate test at 121℃, the ultraviolet absorbance was 0.350.
exceeded the standard value. Although other items were below standard values, the total organic carbon content of the eluate was 48 pp111. The reason why the ultraviolet absorbance and total organic carbon content are higher than that of Example 1 is that 2-hydroxyethyl acrylate has one acrylate group, and PI! G400
This is thought to be due to the weaker binding force compared to diacrylate.

(発明の効果) 本発明は以上のように構成されており、白血球除去フィ
ルターの表面にエチレングリコールの多量体を導入する
ことにより、血液、もしくは血液成分中から血小板は透
過し、白血球のみを効率的かつ安全に選択分離除去可能
であった。また、エチレングリコールの多量体のジアク
リレートを白血球除去フィルター素材に担持させた後、
表面に放射線を照射させることにより表面にエヂレング
= 15 = リコールの多量体を重合させることにより、溶出物が少
なく安定なコーティングが可能であった。
(Effects of the Invention) The present invention is constructed as described above, and by introducing a multimer of ethylene glycol onto the surface of the leukocyte removal filter, platelets from blood or blood components are permeated and only leukocytes are efficiently removed. selective separation and removal was possible in a safe and effective manner. In addition, after supporting leukocyte removal filter material with ethylene glycol polymer diacrylate,
By irradiating the surface with radiation to polymerize a multimer of edge length = 15 = recall on the surface, a stable coating with less eluate was possible.

特許出願人  東洋紡績株式会社 ・−17=Patent applicant: Toyobo Co., Ltd. ・-17=

Claims (2)

【特許請求の範囲】[Claims] (1)ハウジング内に白血球分離材料を収納させてなる
血液もしくは血液の成分と接触し、該血液もしくは血液
成分中から白血球を除去する装置において、血液もしく
は血液成分と接触する白血球分離材料及び/又はハウジ
ング内部の少なくとも1部分がエチレングリコールの多
量体を有する白血球分離装置
(1) In an apparatus for removing leukocytes from blood or blood components by contacting with blood or blood components, the leukocyte separating material is housed in a housing, and/or the leukocyte separating material and/or A leukocyte separation device in which at least a portion of the interior of the housing has an ethylene glycol polymer.
(2)エチレングリコールの多量体のジアクリレートを
白血球除去フィルター素材に担持させた後、放射線を照
射させることにより表面にエチレングリコールの多量体
を重合させる請求項1に記載されている白血球分離材料
の製造方法。
(2) The leukocyte separation material according to claim 1, wherein the leukocyte removal filter material is supported with diacrylate, which is an ethylene glycol polymer, and then irradiated with radiation to polymerize the ethylene glycol polymer on the surface. Production method.
JP31479490A 1990-11-19 1990-11-19 Leucocyte separator and production of leucocyte separating material Pending JPH04187206A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31479490A JPH04187206A (en) 1990-11-19 1990-11-19 Leucocyte separator and production of leucocyte separating material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31479490A JPH04187206A (en) 1990-11-19 1990-11-19 Leucocyte separator and production of leucocyte separating material

Publications (1)

Publication Number Publication Date
JPH04187206A true JPH04187206A (en) 1992-07-03

Family

ID=18057679

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31479490A Pending JPH04187206A (en) 1990-11-19 1990-11-19 Leucocyte separator and production of leucocyte separating material

Country Status (1)

Country Link
JP (1) JPH04187206A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5364533A (en) * 1992-01-10 1994-11-15 Sanwa Kagaku Kenkyusho Co., Ltd. Process for separating serum and plasma
US5647985A (en) * 1994-10-17 1997-07-15 Baxter International Inc. Whole blood leukodepletion and platelet filter
EP0792677A1 (en) * 1996-02-28 1997-09-03 Arbor Technologies, Inc. Leucocyte depleting filter-device, media and method of use
US5728306A (en) * 1994-12-23 1998-03-17 Baxter International Inc. Leukodepletion filter and method for filtering leukocytes from freshly drawn blood
US5972217A (en) * 1994-10-17 1999-10-26 Baxter International Inc. Blood cell separation devices having a membrane with particular coating
US6045701A (en) * 1994-10-17 2000-04-04 Baxter International Inc. Method of filtering a fluid suspension with a membrane having a particular coating
US6648922B2 (en) 1994-10-17 2003-11-18 Baxter International Inc. Method for producing improved medical devices and devices so produced
US6746482B2 (en) 1994-10-17 2004-06-08 Baxter International Inc. Method for producing medical devices and devices so produced
WO2007133147A1 (en) 2006-05-12 2007-11-22 Ibd Column Therapies International Ab Method and means for treating inflammatory bowel disease
JP2010527766A (en) * 2007-05-24 2010-08-19 フジフィルム・マニュファクチュアリング・ヨーロッパ・ベスローテン・フエンノートシャップ Membrane, its manufacturing method and use
JP2010527764A (en) * 2007-05-24 2010-08-19 フジフィルム・マニュファクチュアリング・ヨーロッパ・ベスローテン・フエンノートシャップ Membrane containing oxyethylene groups
JP2010527765A (en) * 2007-05-24 2010-08-19 フジフィルム・マニュファクチュアリング・ヨーロッパ・ベスローテン・フエンノートシャップ Membrane containing oxyethylene groups

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5364533A (en) * 1992-01-10 1994-11-15 Sanwa Kagaku Kenkyusho Co., Ltd. Process for separating serum and plasma
US6746482B2 (en) 1994-10-17 2004-06-08 Baxter International Inc. Method for producing medical devices and devices so produced
US7422606B2 (en) 1994-10-17 2008-09-09 Edwards Lifesciences Corporation Medical devices and products having coatings applied thereto
US5647985A (en) * 1994-10-17 1997-07-15 Baxter International Inc. Whole blood leukodepletion and platelet filter
US5795483A (en) * 1994-10-17 1998-08-18 Baxter International Inc. Method of separating leukocytes from blood cells using a leukodepletion filter
US6648922B2 (en) 1994-10-17 2003-11-18 Baxter International Inc. Method for producing improved medical devices and devices so produced
US5972217A (en) * 1994-10-17 1999-10-26 Baxter International Inc. Blood cell separation devices having a membrane with particular coating
US6045701A (en) * 1994-10-17 2000-04-04 Baxter International Inc. Method of filtering a fluid suspension with a membrane having a particular coating
US5885457A (en) * 1994-12-23 1999-03-23 Baxter International Inc. Filtration media for filtering leukocytes from freshly drawn blood
US5728306A (en) * 1994-12-23 1998-03-17 Baxter International Inc. Leukodepletion filter and method for filtering leukocytes from freshly drawn blood
EP0792677A1 (en) * 1996-02-28 1997-09-03 Arbor Technologies, Inc. Leucocyte depleting filter-device, media and method of use
WO2007133147A1 (en) 2006-05-12 2007-11-22 Ibd Column Therapies International Ab Method and means for treating inflammatory bowel disease
JP2010527766A (en) * 2007-05-24 2010-08-19 フジフィルム・マニュファクチュアリング・ヨーロッパ・ベスローテン・フエンノートシャップ Membrane, its manufacturing method and use
JP2010527764A (en) * 2007-05-24 2010-08-19 フジフィルム・マニュファクチュアリング・ヨーロッパ・ベスローテン・フエンノートシャップ Membrane containing oxyethylene groups
JP2010527765A (en) * 2007-05-24 2010-08-19 フジフィルム・マニュファクチュアリング・ヨーロッパ・ベスローテン・フエンノートシャップ Membrane containing oxyethylene groups

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