JP2003245346A - Blood processing device of hollow fiber membrane type and manufacturing method therefor - Google Patents

Blood processing device of hollow fiber membrane type and manufacturing method therefor

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Publication number
JP2003245346A
JP2003245346A JP2002047285A JP2002047285A JP2003245346A JP 2003245346 A JP2003245346 A JP 2003245346A JP 2002047285 A JP2002047285 A JP 2002047285A JP 2002047285 A JP2002047285 A JP 2002047285A JP 2003245346 A JP2003245346 A JP 2003245346A
Authority
JP
Japan
Prior art keywords
hollow fiber
fiber membrane
resin
blood
urea
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
JP2002047285A
Other languages
Japanese (ja)
Inventor
Yoshio Enomoto
義雄 榎本
Kimiaki Nishimura
公美章 西村
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.)
Asahi Kasei Medical Co Ltd
Original Assignee
Asahi Medical 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 Asahi Medical Co Ltd filed Critical Asahi Medical Co Ltd
Priority to JP2002047285A priority Critical patent/JP2003245346A/en
Publication of JP2003245346A publication Critical patent/JP2003245346A/en
Pending legal-status Critical Current

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  • External Artificial Organs (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a blood processing device which shows an excellent residual blood performance by suppressing activation of blood at the time of the flow and by reducing the amount of residual blood after use, and a manufacturing method therefor. <P>SOLUTION: A bundle of cellulosic hollow fiber membranes formed with a resin embedding part by embedding and securing the end part of the bundle of the hollow fiber membranes with a resin is contained in the blood processing device. The hollow fiber membranes are opened by cutting at least one end of the resin embedding part, and the cross section of the resin embedding part of the hollow fiber membranes is treated with a urea organic solvent solution and is impregnated with urea. Urea is fixed to the cross-section by an irradiation treatment. Preferably, the hollow fiber membrane of a regenerated cellulose should be used, and the ratio of the internal diameter of the opening part of the hollow fiber membrane at the cross-section of the resin embedding part in a dry condition to the internal diameter in a wet condition should be set as 'Dw/Dd=1.0-1.1'. (Dw stands for the inner diameter of the hollow fiber at the cross-section of the resin embedding part in a wet condition with water. Dd stands for the inner diameter of the hollow fiber in a dry condition before being wet with water.) The manufacturing method is to perform the irradiation treatment of the cross-section of the resin embedding part of the hollow fiber membranes after it is impregnated with urea by treating it with the organic solvent urea solution. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、新規な中空糸膜型
血液処理装置及びその製造方法に関する。本発明の中空
糸膜血液処理装置は、残血の少ない血液浄化器用とし
て、医療分野等において好適に用いることができる。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a novel hollow fiber membrane type blood treatment apparatus and a method for manufacturing the same. INDUSTRIAL APPLICABILITY The hollow fiber membrane blood processing apparatus of the present invention can be suitably used in a medical field or the like for a blood purifier with less residual blood.

【0002】[0002]

【従来の技術】中空糸膜型血液処理装置は、血液透析、
血液濾過ないし血漿分離等の血液中の特定成分の分離に
使用されている。中空糸膜型血液処理装置では、ヘッダ
ー部及び中空糸部での血液の流動がスムーズに行われ、
かつ、血液と部材の接触による血液成分の活性化が起こ
らないことが望ましい。そのような血液の流動性のよい
血液浄化器では、使用後の血液浄化器内に残留する血液
量、いわゆる残血量を減少させることができる。
2. Description of the Related Art Hollow fiber membrane blood treatment equipment is used for hemodialysis,
It is used for separation of specific components in blood such as blood filtration and plasma separation. In the hollow fiber membrane blood processing device, the flow of blood in the header part and the hollow fiber part is smoothly performed,
Moreover, it is desirable that the activation of the blood component does not occur due to the contact between the blood and the member. In such a blood purifier with good fluidity of blood, the amount of blood remaining in the blood purifier after use, that is, the amount of residual blood can be reduced.

【0003】例えば、血液の流動状態を改善する技術と
して、特開昭57−86362号公報では、中空糸膜型
血液処理装置の樹脂固定部切断面における中空糸膜の内
径を拡大し、血液導入部及び血液導出部の開口度を大き
くして血液の流動抵抗を改善した、残血の少ない中空糸
膜型血液処理装置が開示されている。しかし、この装置
は、合成膜を使用する場合、湿潤による中空糸膜の膨潤
が実質的に認められないために、その効果を発揮できる
が、再生セルロースのように、血液や水等で膨潤する素
材の場合は、中空糸膜の膜厚部の膨潤による開口部の狭
小化が著しい。したがって、セルロース系中空糸膜を使
用する場合には、樹脂包埋部における中空糸膜の内径サ
イズを乾燥状態と同じか又はさらに拡大した状態に維持
するのは困難であり、十分な開口度及び残血を減少させ
る効果が得られていない。開口度を大きくする手段とし
て、膨潤による開口度の減少を防ぐために、乾燥状態で
の内径が大きい中空糸を使用することも可能である
が、中空糸膜の内径を大きくすることは、クリアランス
性能の低下及び中空糸生産性の低下等の問題があり、そ
の大きさに限界がある。
For example, as a technique for improving the flow state of blood, Japanese Patent Application Laid-Open No. 57-86362 discloses that the inner diameter of the hollow fiber membrane at the cut surface of the resin fixing portion of the hollow fiber membrane blood processing apparatus is enlarged to introduce blood. There is disclosed a hollow fiber membrane-type blood treatment device with less residual blood, in which the flow resistance of blood is improved by increasing the opening degree of the blood discharge part and the blood discharge part. However, when a synthetic membrane is used, this device can exert its effect because swelling of the hollow fiber membrane due to wetting is not substantially observed, but it swells with blood or water like regenerated cellulose. In the case of a raw material, the narrowing of the opening due to the swelling of the film thickness portion of the hollow fiber membrane is remarkable. Therefore, when using a cellulosic hollow fiber membrane, it is difficult to maintain the inner diameter size of the hollow fiber membrane in the resin-embedded portion in the same state as in the dry state or in a state where the hollow fiber membrane is further expanded, and a sufficient opening degree and Not effective in reducing residual blood. As a means of increasing the opening degree, it is possible to use a hollow fiber membrane having a large inner diameter in a dry state in order to prevent a decrease in the opening degree due to swelling. There are problems such as deterioration in performance and hollow fiber productivity, and their size is limited.

【0004】上記従来の血液処理装置用のセルロース系
中空糸膜の問題点を図に基づいて説明する。図1は、従
来から用いられている血液処理装置用のセルロース系中
空糸膜とそれを包埋固定する樹脂の乾燥状態における説
明図(模式図)であり、図2は、同じ血液処理装置用の
セルロース系中空糸膜とその包埋固定樹脂の湿潤状態に
おける説明図(模式図)である。図1及び図2におい
て、1は中空糸膜を包埋固定する樹脂、2は中空糸膜の
樹脂包埋部、3は中空糸膜の非樹脂包埋部、4は樹脂の
切断面、5は中空糸膜の樹脂包埋部の切断面である。図
1と図2を対比すると、乾燥状態の中空糸膜(図1)に
比べて湿潤状態の中空糸膜(図2)では、中空糸膜が膨
潤してその膜厚が大きくなっているが、樹脂包埋部2で
は、径方向への膨潤がこれを包埋固定する樹脂1によっ
て規制されるため、中空糸膜の切断面5の内径寸法が縮
小しており、一方、非樹脂包埋部3では、膨潤が規制さ
れないため、その膜厚及び内径寸法が大きく拡大してい
ることが理解できる。
The problems of the above-mentioned conventional cellulose-based hollow fiber membranes for blood processing apparatuses will be described with reference to the drawings. FIG. 1 is an explanatory view (schematic diagram) of a conventionally used cellulose-based hollow fiber membrane for a blood processing apparatus and a resin for embedding and fixing the hollow-fiber membrane, and FIG. 2 is for the same blood processing apparatus. FIG. 3 is an explanatory diagram (schematic diagram) of the cellulosic hollow fiber membrane and its embedded fixing resin in a wet state. 1 and 2, 1 is a resin for embedding and fixing a hollow fiber membrane, 2 is a resin-embedded portion of the hollow fiber membrane, 3 is a non-resin-embedded portion of the hollow fiber membrane, 4 is a cut surface of the resin, 5 Is a cut surface of the resin-embedded portion of the hollow fiber membrane. Comparing FIG. 1 and FIG. 2, in the hollow fiber membrane in the wet state (FIG. 2), the hollow fiber membrane swells and the thickness becomes larger than that in the dry state (FIG. 1). In the resin-embedded portion 2, since the swelling in the radial direction is restricted by the resin 1 that embeds and fixes the resin-embedded portion 2, the inner diameter dimension of the cut surface 5 of the hollow fiber membrane is reduced, while the non-resin-embedded portion It can be understood that the thickness and the inner diameter of the portion 3 are greatly expanded because the swelling is not regulated.

【0005】したがって、樹脂包埋部における、このよ
うな中空糸膜の形態では、中空糸膜への血液導入の際に
流れの急激な縮少が起こり、かつ、血液導出の際に流れ
の急激な拡大が起こる。そのために、血液の乱れが生じ
やすくなり、血液成分の活性化を引き起こす。このこと
が、セルロース系中空糸膜型血液処理装置の残血性を悪
くしている要因の一つであった。
Therefore, in the form of such a hollow fiber membrane in the resin-embedded portion, a rapid reduction of the flow occurs at the time of introducing blood into the hollow fiber membrane, and a sharp flow of the flow occurs at the time of drawing blood. Expansion occurs. As a result, blood disorder is likely to occur, causing activation of blood components. This is one of the factors that deteriorate the residual blood property of the cellulosic hollow fiber membrane blood treatment apparatus.

【0006】[0006]

【発明が解決しようとする課題】上記の状況に鑑み、本
発明は、従来技術においては十分に達成されていなかっ
たセルロース系中空糸膜を内蔵する血液処理装置の、中
空糸膜の血液導入部切断面及び血液導出部切断面におけ
る中空糸膜の湿潤による内径縮小を抑制し、中空糸膜の
切断面開口部にテーパー状の形状を付与することによ
り、血液流動抵抗を改善し、かつ、血液の流動時の活性
化を抑制し、使用後の血液処理装置内に残留する血液
量、すなわち残血量を減少させた、すぐれた残血特性を
有する中空糸膜型血液処理装置及びその製造方法を提供
することを課題とする。
SUMMARY OF THE INVENTION In view of the above situation, the present invention provides a blood introducing portion of a hollow fiber membrane of a blood processing apparatus incorporating a cellulosic hollow fiber membrane, which has not been sufficiently achieved in the prior art. Suppressing the inner diameter reduction due to the wetting of the hollow fiber membrane on the cut surface and the blood discharge portion cut surface, and improving the blood flow resistance by imparting a tapered shape to the cut surface opening of the hollow fiber membrane, and blood Hollow fiber membrane blood treatment apparatus having excellent residual blood characteristics, which suppresses the activation of blood during activation and reduces the amount of blood remaining in the blood treatment apparatus after use, that is, residual blood volume, and a method for producing the same The challenge is to provide.

【0007】[0007]

【課題を解決するための手段】上記の課題を解決するた
めに、本発明者らは、中空糸膜の樹脂包埋部の血液と接
触する切断面を尿素の有機溶媒溶液で処理して尿素を含
浸させた後、該切断面を照射することにより、該切断面
における中空糸膜内径の拡大及び膜厚部の水ないし血液
含浸による膨潤が抑制されることを見いだし、本発明に
到達した。
In order to solve the above-mentioned problems, the inventors of the present invention treated the cut surface of the hollow fiber membrane-embedded portion in contact with blood with a solution of urea in an organic solvent to form urea. By impregnating the cut surface and then irradiating the cut surface, it was found that expansion of the inner diameter of the hollow fiber membrane at the cut surface and swelling of the film thickness portion due to water or blood impregnation were suppressed, and the present invention was reached.

【0008】すなわち、本発明のうち請求項1に記載の
発明は、中空糸膜束の端部を樹脂で包埋固定して樹脂包
埋部を形成してあるセルロース系中空糸膜束を内蔵し、
少なくとも一方の樹脂包埋部の端部を切断して中空糸膜
を開口させてあると共に、該中空糸膜の樹脂包埋部の切
断面を尿素の有機溶媒溶液で処理して尿素を含浸させて
あり、かつ、照射処理をしてあることを特徴とする中空
糸膜型血液処理装置である。
That is, the invention according to claim 1 of the present invention has a built-in cellulosic hollow fiber membrane bundle in which an end portion of the hollow fiber membrane bundle is embedded and fixed in a resin to form a resin-embedded portion. Then
At least one end of the resin-embedded portion is cut to open the hollow fiber membrane, and the cut surface of the resin-embedded portion of the hollow fiber membrane is treated with an organic solvent solution of urea to impregnate it with urea. The hollow fiber membrane-type blood treatment apparatus is characterized in that it has been subjected to irradiation treatment.

【0009】本発明のうち請求項2に記載の発明は、請
求項1に記載の装置であって、セルロース系中空糸膜束
の素材が、再生セルロースである中空糸膜型血液処理装
置である。また、請求項3に記載の発明は、請求項1又
は2に記載の装置であって、中空糸を包埋固定する樹脂
が、ポリウレタン樹脂である中空糸膜型血液処理装置で
ある。
The second aspect of the present invention is the apparatus according to the first aspect, wherein the material of the cellulosic hollow fiber membrane bundle is a regenerated cellulose. . The invention according to claim 3 is the device according to claim 1 or 2, wherein the resin for embedding and fixing the hollow fiber is a polyurethane resin.

【0010】本発明のうち請求項4に記載の発明は、請
求項1から3のいずれかに記載の装置であって、樹脂包
埋部の切断面における中空糸膜の開口部の乾燥時と湿潤
時の内径比が以下の範囲である中空糸膜型血液処理装置
である。 Dw/Dd=1.0〜1.1 ここで、Dwは、樹脂包埋部切断面における水湿潤状態
の中空糸膜の内径を、Ddは、水湿潤状態前の乾燥状態
での中空糸膜の内径を示す。
A fourth aspect of the present invention is the apparatus according to any one of the first to third aspects, wherein the opening of the hollow fiber membrane on the cut surface of the resin-embedded portion is dried. The hollow fiber membrane-type blood processing device has an inner diameter ratio in the following range when wet. Dw / Dd = 1.0 to 1.1 Here, Dw is the inner diameter of the hollow fiber membrane in the water-wet state on the cut surface of the resin-embedded portion, and Dd is the hollow fiber membrane in the dry state before the water-wet state. Indicates the inner diameter of.

【0011】本発明のうち請求項5に記載の発明は、中
空糸膜束の端部を樹脂で包埋固定して樹脂包埋部を形成
してあるセルロース系中空糸膜束を内蔵し、少なくとも
一方の樹脂包埋部の端部を切断して中空糸膜を開口させ
ると共に、該中空糸膜の樹脂包埋部の切断面を尿素の有
機溶媒溶液で処理して尿素を含浸させた後、照射処理す
ることを特徴とする中空糸膜型血液処理装置の製造方法
である。
According to a fifth aspect of the present invention, the cellulosic hollow fiber membrane bundle in which the end portion of the hollow fiber membrane bundle is embedded and fixed in a resin to form a resin-embedded portion is incorporated, After cutting at least one end of the resin-embedded portion to open the hollow fiber membrane, after treating the cut surface of the resin-embedded portion of the hollow fiber membrane with an organic solvent solution of urea to impregnate urea The method for manufacturing a hollow fiber membrane-type blood treatment device is characterized in that irradiation treatment is performed.

【0012】本発明のうち請求項6に記載の発明は、請
求項5に記載の装置の製造方法であって、尿素の有機溶
媒溶液が、メタノール溶液である中空糸膜型血液処理装
置の製造方法である。
The invention according to claim 6 of the present invention is the method for manufacturing the device according to claim 5, wherein the organic solvent solution of urea is a methanol solution. Is the way.

【0013】本発明のうち請求項7に記載の発明は、請
求項5又は6に記載の装置の製造方法であって、尿素溶
液の濃度が、1〜20重量%である中空糸膜型血液処理
装置の製造方法である。
The invention according to claim 7 of the present invention is the method for manufacturing the device according to claim 5 or 6, wherein the concentration of the urea solution is 1 to 20% by weight. It is a manufacturing method of a processing apparatus.

【0014】本発明のうち請求項8に記載の発明は、請
求項5から7のいずれかに記載の装置の製造方法であっ
て、照射処理として、紫外線照射をすることとした中空
糸膜型血液処理装置の製造方法である。
The invention according to claim 8 of the present invention is the method for manufacturing the device according to any one of claims 5 to 7, wherein the irradiation is carried out by ultraviolet ray irradiation. It is a manufacturing method of a blood processing apparatus.

【0015】[0015]

【発明の実施の形態】以下、本発明について具体的に説
明する。本発明において、「中空糸膜」とは、膜機能を
有する中空糸状の細管のことである。また、本発明にお
いて、「%」の表示は、特に断らない限り、重量割合を
示す。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below. In the present invention, the “hollow fiber membrane” is a hollow fiber thin tube having a membrane function. In addition, in the present invention, “%” is a weight ratio unless otherwise specified.

【0016】セルロース系中空糸膜束を血液処理装置の
本体ケースに収納した後、該中空糸膜束の両端を樹脂で
本体ケースに包埋し固定する。この包埋固定の方法は、
公知の方法のいずれでもよい。本発明で用いる中空糸膜
の素材は、本発明の固定方法によって湿潤時の膨潤を抑
制できる素材であれば、特に限定されないが、再生セル
ロース等の、従来の方法では血液での湿潤により膨潤す
る素材を積極的に使用することが好ましい。包埋樹脂と
しては、ポリウレタン樹脂が一般的に使用される。
After storing the cellulosic hollow fiber membrane bundle in the main body case of the blood processing apparatus, both ends of the hollow fiber membrane bundle are embedded in the main body case with resin and fixed. This embedded fixation method is
Any known method may be used. The material of the hollow fiber membrane used in the present invention is not particularly limited as long as it is a material capable of suppressing swelling when wet by the fixing method of the present invention, but swells by wetness with blood in a conventional method such as regenerated cellulose. It is preferable to actively use the material. Polyurethane resin is generally used as the embedding resin.

【0017】上記のように本体ケースに内蔵した中空糸
膜束の端部を切断し、中空糸膜の少なくとも片端を開口
させる。次いで、該開口した切断面に尿素を含浸させ
る。尿素の含浸方法としては、尿素の有機溶媒溶液に上
記切断面を浸漬する方法や尿素の有機溶媒溶液を噴霧す
る方法等があるが、処理工程の簡便性を考慮すると、噴
霧法が好ましい。この際、尿素を溶解する溶媒として
は、樹脂を溶解せず、かつ中空糸膜の素材と親和性があ
り、容易に中空糸膜内へ含浸できることが必要である。
また、揮発しやすい溶媒や水洗等で容易に除去できるも
のが好ましい。そのような条件を充たす有機溶媒として
は、例えば、メタノールやエタノール等を挙げることが
できる。しかし、本発明では、これらに限定されるもの
ではない。
As described above, the end portion of the hollow fiber membrane bundle contained in the main body case is cut to open at least one end of the hollow fiber membrane. Then, the opened cut surface is impregnated with urea. As a method for impregnating urea, there are a method of immersing the cut surface in an organic solvent solution of urea, a method of spraying an organic solvent solution of urea, and the like, but the spraying method is preferable in view of simplicity of the treatment process. At this time, the solvent that dissolves urea must be one that does not dissolve the resin, has an affinity for the material of the hollow fiber membrane, and can be easily impregnated into the hollow fiber membrane.
Further, a solvent that easily volatilizes or a solvent that can be easily removed by washing with water is preferable. Examples of the organic solvent that satisfies such conditions include methanol and ethanol. However, the present invention is not limited to these.

【0018】尿素溶液の濃度は、中空糸膜の素材によっ
て異なるため、これらの素材に応じて適正化することが
好ましい。例えば、再生セルロースの中空糸膜を使用す
る場合は、尿素のメタノール溶液のとき、1〜20%の
範囲が好ましい。1%よりも低い濃度の場合は、1回の
浸漬のみでは十分な付着量が得られず、付着効果が上が
らない。また、1%よりも低い濃度の場合、噴霧法で十
分な含浸量を得るためには繰り返して噴霧する必要があ
るが、繰り返し噴霧すると、尿素溶液の樹脂内への浸入
量が多くなり、その溶媒の除去が煩雑になる。一方、2
0%以上の濃度の場合は、尿素溶液処理後の中空糸膜の
切断面に尿素が析出し、その後の照射処理時のエネルギ
ー吸収効率が悪くなって、照射に長時間を要する等の不
都合が生じる。
Since the concentration of the urea solution varies depending on the material of the hollow fiber membrane, it is preferable to optimize it according to these materials. For example, when a hollow fiber membrane of regenerated cellulose is used, it is preferably in the range of 1 to 20% when using a methanol solution of urea. When the concentration is lower than 1%, a sufficient amount of adhesion cannot be obtained by only one dipping, and the adhesion effect cannot be improved. Further, when the concentration is lower than 1%, it is necessary to repeat spraying in order to obtain a sufficient impregnation amount by the spraying method, but when spraying repeatedly, the amount of the urea solution penetrating into the resin increases, and Solvent removal becomes complicated. On the other hand, 2
When the concentration is 0% or more, urea is deposited on the cut surface of the hollow fiber membrane after the urea solution treatment, the energy absorption efficiency at the time of the subsequent irradiation treatment is deteriorated, and irradiation takes a long time. Occurs.

【0019】尿素の有機溶媒溶液で処理した後、中空糸
膜内径の湿潤による縮小を抑制するために、含浸した尿
素をセルロースに固定するための照射を行う。この照射
処理には、遠赤外線、ガンマ線、紫外線、レーザー光線
等を用いることができるが、取り扱い性や固定処理の容
易さから、紫外線照射が好ましい。紫外線で照射して固
定する場合は、紫外線の波長は、エキシマランプを使用
して得られる170nm近辺から370nmまでであれ
ば特に限定されないが、中空糸膜素材及び包埋樹脂の紫
外線吸収特性を考慮して決定するのが好ましい。例え
ば、再生セルロースとポリウレタン樹脂の組み合わせの
場合、医療用であることを考慮すると、殺菌用に使用さ
れる253.7nm以上の波長とするのが好ましい。照
射条件は、紫外線の照射強度、照射量、照射する紫外線
の波長、照射距離、紫外線発生光源の種類や固定用樹脂
の種類等によって、適正な条件を定めるのが好ましい。
例えば、再生セルロースの中空糸膜束を使用し、ポリウ
レタン樹脂で固定する血液処理装置の場合は、照射強度
は1〜29nmW/cm2 の範囲で5〜90分間程度の
照射でよい。照射強度が1mW/cm2 よりも弱いと処
理に長時間を要する。また、十分な膨潤抑制効果が得ら
れない。20mW/cm2 よりも強いと、ポリウレタン
樹脂表面に化学的変質が起こりやすくなり、好ましくな
い影響を惹起することがある。また、レーザー光線を照
射して固定する場合、炭酸ガスレーザーが好ましく、そ
の波長は10.6μmある。照射条件は、レーザー出
力、照射距離、照射雰囲気ないし照射速度等を変更する
ことにより広い範囲で適正化できるが、中空糸膜素材の
耐レーザー光線特性を考慮して決定するのが好ましい。
例えば、セルロースの場合、レーザー出力は10〜10
0ワットの範囲が好ましい。また、照射距離は、出力及
び照射雰囲気条件によって適正化することが必要である
が、例えば、50ワットの場合、20〜50cmの距離
が好ましい。また、照射雰囲気は、中空糸膜及び中空糸
固定樹脂の酸化・劣化を防ぐために窒素ガス等の不活性
気体を流しながら照射するのが好ましい。ただし、これ
らの条件は、補完的に作用するため、本発明の範囲は、
これらの条件範囲に限定されるものではない。また、照
射エネルギーが大き過ぎると、固定樹脂の溶融、変形等
が起こりやすくなって、血液の活性抑制効果が得られな
くなる。
After the treatment with the organic solvent solution of urea, irradiation for fixing the impregnated urea to the cellulose is performed in order to suppress the reduction of the inner diameter of the hollow fiber membrane due to wetting. Far infrared rays, gamma rays, ultraviolet rays, laser beams and the like can be used for this irradiation treatment, but ultraviolet irradiation is preferable from the viewpoint of handleability and ease of fixing treatment. When irradiating and fixing with ultraviolet rays, the wavelength of ultraviolet rays is not particularly limited as long as it is around 170 nm obtained using an excimer lamp to 370 nm, but the ultraviolet absorption characteristics of the hollow fiber membrane material and the embedding resin are taken into consideration. It is preferable to make the above decision. For example, in the case of a combination of regenerated cellulose and a polyurethane resin, it is preferable that the wavelength is 253.7 nm or more, which is used for sterilization, considering that it is for medical use. It is preferable to determine appropriate irradiation conditions depending on the irradiation intensity and irradiation amount of ultraviolet rays, the wavelength of ultraviolet rays to be irradiated, the irradiation distance, the type of ultraviolet ray generating light source, the type of fixing resin, and the like.
For example, in the case of a blood processing apparatus in which a hollow fiber membrane bundle of regenerated cellulose is used and fixed with a polyurethane resin, the irradiation intensity may be in the range of 1 to 29 nmW / cm 2 for about 5 to 90 minutes. If the irradiation intensity is weaker than 1 mW / cm 2 , it takes a long time to process. Moreover, a sufficient swelling suppressing effect cannot be obtained. If the strength is higher than 20 mW / cm 2 , chemical deterioration is likely to occur on the surface of the polyurethane resin, which may cause undesirable effects. Further, in the case of irradiating and fixing with a laser beam, a carbon dioxide gas laser is preferable and its wavelength is 10.6 μm. The irradiation conditions can be optimized in a wide range by changing the laser output, the irradiation distance, the irradiation atmosphere or the irradiation speed, etc., but it is preferably determined in consideration of the laser beam resistance property of the hollow fiber membrane material.
For example, in the case of cellulose, the laser output is 10 to 10
The 0 watt range is preferred. Further, the irradiation distance needs to be optimized depending on the output and irradiation atmosphere conditions, but for example, in the case of 50 watts, a distance of 20 to 50 cm is preferable. Further, the irradiation atmosphere is preferably irradiation while flowing an inert gas such as nitrogen gas in order to prevent oxidation and deterioration of the hollow fiber membrane and the hollow fiber fixing resin. However, since these conditions act complementarily, the scope of the present invention is
It is not limited to these condition ranges. Further, if the irradiation energy is too large, the fixing resin is likely to melt, deform, etc., and the blood activity suppressing effect cannot be obtained.

【0020】中空糸膜に含浸させる尿素の量は、中空糸
膜内部及びそれを包埋する樹脂へ浸入している尿素の量
で規定されるが、ポリウレタン樹脂を使用する場合、樹
脂及び中空糸膜の切断面から0.1cm以上の範囲にわ
たって、前記の濃度の尿素溶液が含浸されていればよ
い。また、尿素の有機溶媒溶液処理から照射処理までの
時間は、特に限定されないが、室温状態で保管した場
合、有機溶媒溶液処理直後から2週間以内であれば十分
な内径縮小抑制効果が認められる。
The amount of urea with which the hollow fiber membrane is impregnated is defined by the amount of urea that has penetrated into the hollow fiber membrane and the resin that embeds it. When a polyurethane resin is used, the resin and the hollow fiber are used. The urea solution having the above concentration may be impregnated over a range of 0.1 cm or more from the cut surface of the membrane. Further, the time from the treatment with the organic solvent solution of urea to the irradiation treatment is not particularly limited, but when stored at room temperature, a sufficient effect of suppressing the inner diameter reduction is recognized within 2 weeks immediately after the treatment with the organic solvent solution.

【0021】尿素の有機溶媒溶液処理及び照射処理をし
た後、残留溶媒及び遊離尿素等を除去するために、その
除去工程を設けることが好ましい。その除去方法として
は、例えば、水による洗浄除去法が適用できる。
After the treatment of the organic solvent with urea and the irradiation treatment, it is preferable to provide a removing step for removing the residual solvent and free urea. As the removing method, for example, a washing and removing method using water can be applied.

【0022】本発明に係る血液処理装置は、中空糸膜切
断面を含む樹脂包埋部の切断面を尿素の有機溶媒溶液、
例えば、尿素のメタノール溶液で処理して尿素を含浸さ
せた後、照射することにより達成されるが、中空糸膜の
湿潤による内径の縮小を抑制する作用について、以下の
2つの機作を推測できる。 (1)中空糸膜を含む樹脂切断面にメタノール等の有機
溶媒が含浸されることにより、樹脂、特に中空糸膜を包
埋している近辺の樹脂が柔軟になり、かつ、メタノール
等の有機溶媒による中空糸膜の内径及び膜厚部の膨潤が
起こる。この際、メタノール等の有機溶媒では、膜厚部
の膨潤が少なく、そのため、内径の拡大が起こる。この
中空糸膜の膨潤による内径の拡大により、切断面開口部
の柔らかくなった樹脂が押し広げられ、中空糸膜の内径
がテーパー状に拡大する。 (2)上記膨潤状態の中空糸膜を照射処理することによ
り、中空糸膜と中空糸膜に含浸された尿素の化学反応が
起こり、湿潤による中空糸膜のセルロースの膨潤が抑制
される構造に変化するものと推定される。
In the blood processing apparatus according to the present invention, the cut surface of the resin-embedded portion including the cut surface of the hollow fiber membrane is an organic solvent solution of urea,
For example, the following two mechanisms can be inferred for the effect of suppressing the reduction of the inner diameter due to the wetting of the hollow fiber membrane, which is achieved by irradiating after treating with a methanol solution of urea to impregnate urea. . (1) By impregnating the cut surface of the resin containing the hollow fiber membrane with an organic solvent such as methanol, the resin, particularly the resin in the vicinity of the hollow fiber membrane, becomes flexible, and the organic material such as methanol Swelling of the inner diameter and the membrane portion of the hollow fiber membrane due to the solvent occurs. At this time, with an organic solvent such as methanol, the swelling of the film thickness portion is small, so that the inner diameter increases. Due to the expansion of the inner diameter due to the swelling of the hollow fiber membrane, the softened resin in the opening of the cut surface is spread and the inner diameter of the hollow fiber membrane is expanded in a tapered shape. (2) By subjecting the hollow fiber membrane in the swollen state to irradiation treatment, a chemical reaction occurs between the hollow fiber membrane and the urea impregnated in the hollow fiber membrane, so that the swelling of cellulose in the hollow fiber membrane due to wetting is suppressed. It is estimated to change.

【0023】本発明は、上記2点の機作により、セルロ
ース系中空糸膜の湿潤による膨潤を抑制しているものと
推定される。したがって、その反応の進行程度により湿
潤時の膨潤状態は変化する。前の中空糸膜が走行してい
るローラー等の表面に尿素の有機溶媒溶液を供給して中
空糸膜と接触させる方法等がある。ただし、赤外線分光
光度計で測定した場合、5.0〜6.0μmの波長範囲
で吸収パターンの変化が認められるが、特異吸収波長を
有さないために、生成している結合基は明確では無い。
It is presumed that the present invention suppresses the swelling of the cellulosic hollow fiber membrane due to the wetting by the above two mechanisms. Therefore, the swelling state when wet changes depending on the progress of the reaction. There is a method in which an organic solvent solution of urea is supplied to the surface of a roller or the like on which the previous hollow fiber membrane is running to bring it into contact with the hollow fiber membrane. However, when measured with an infrared spectrophotometer, a change in the absorption pattern is observed in the wavelength range of 5.0 to 6.0 μm, but since it does not have a specific absorption wavelength, the bonding group produced is not clear. There is no.

【0024】本発明の血液処理装置は、包埋樹脂及び中
空糸膜の樹脂包埋部の切断面を尿素の有機溶媒溶液で処
理して、有機溶媒及び尿素を包埋樹脂及び中空糸膜の樹
脂包埋部に含浸させることにより、中空糸膜の内径が拡
大し、その後の照射処理により膜厚部の膨潤による内径
縮小が抑制されるが、内径の縮小抑制効果は、Dw/D
d=1.0〜1.1の範囲で、残血性の改善効果が認め
られた。ただし、Dwは、中空糸膜の樹脂包埋部切断面
における水湿潤状態の内径を、また、Ddは、その樹脂
包埋部切断面における水湿潤前の乾燥状態の内径を示
す。Dw/Ddが1.0よりも小さいと、効果が不十分
であった。一方、上限は大きいほど好ましいと思われる
が、本発明の製造方法では、1.1までの値を確認する
ことができた。
In the blood treatment apparatus of the present invention, the cut surface of the resin-embedded portion of the embedding resin and the hollow fiber membrane is treated with an organic solvent solution of urea, and the organic solvent and urea are treated with the embedding resin and the hollow fiber membrane. By impregnating the resin-embedded portion, the inner diameter of the hollow fiber membrane is increased, and the subsequent irradiation treatment suppresses the inner diameter reduction due to the swelling of the membrane portion, but the inner diameter reduction suppression effect is Dw / D.
In the range of d = 1.0 to 1.1, the effect of improving the residual blood property was recognized. However, Dw represents the inner diameter of the hollow surface of the resin-embedded portion in the water-wet state, and Dd represents the inner diameter of the resin-embedded portion in the dry state before wetting. When Dw / Dd was smaller than 1.0, the effect was insufficient. On the other hand, although it seems that the larger the upper limit is, the more preferable, but in the production method of the present invention, values up to 1.1 could be confirmed.

【0025】本発明の中空糸膜の湿潤時の状態を図に基
づいて説明する。図3は、本発明に係る血液処理装置用
のセルロース系中空糸膜とそれを包埋固定する樹脂の湿
潤状態における説明図(模式図)である。図3で用いる
符号は、図1及び図2と同じであり、1は中空糸膜を包
埋固定する樹脂、2は中空糸膜の樹脂包埋部、3は中空
糸膜の非樹脂包埋部、4は樹脂の切断面、5は中空糸膜
の樹脂包埋部の切断面を示す。前記の図1・図2(従来
の中空糸膜)とこの図3(本発明の中空糸膜)を対比す
ると、湿潤状態において、図3の中空糸膜の樹脂包埋部
2は、図2の中空糸膜の樹脂包埋部2と同じようには膨
潤せず、図3の中空糸膜の切断面5は、図2の中空糸膜
の切断面5よりもテーパー状に拡大した状態となってい
る。図3の中空糸膜の切断面5は、図1の中空糸膜の切
断面5(従来法による乾燥時のもの)とほとんど変わり
がない。この理由は、包埋樹脂1の切断面4及び中空糸
膜の樹脂包埋部2の切断面5を尿素の有機溶媒溶液で処
理する際に、樹脂1へ浸入した有機溶媒の作用で樹脂1
が軟らかくなり、同時に中空糸膜の樹脂包埋部2の膜厚
部に浸入した有機溶媒の膨潤作用で、中空糸膜の切断面
5の内径が拡大され、有機溶媒と共に中空糸膜に浸入し
た尿素の作用で拡大された状態が維持される。この際、
膜厚部の有機溶媒による膨潤はほとんど起こらないと考
えられる。その後の照射処理により、尿素と中空糸膜の
間で反応が起こり、湿潤化による中空糸膜の膜厚の膨潤
が抑制される構造が形成され、湿潤化後は、内径がテー
パー状に拡大した形状が実現されると考えられる。
The wet state of the hollow fiber membrane of the present invention will be described with reference to the drawings. FIG. 3 is an explanatory diagram (schematic diagram) in a wet state of a cellulosic hollow fiber membrane for a blood processing apparatus according to the present invention and a resin for embedding and fixing the same. Reference numerals used in FIG. 3 are the same as those in FIGS. 1 and 2, 1 is a resin for embedding and fixing the hollow fiber membrane, 2 is a resin embedding portion of the hollow fiber membrane, and 3 is a non-resin embedding of the hollow fiber membrane. Reference numeral 4 denotes a cut surface of the resin, and 5 denotes a cut surface of the resin-embedded portion of the hollow fiber membrane. Comparing FIG. 1 and FIG. 2 (conventional hollow fiber membrane) with FIG. 3 (hollow fiber membrane of the present invention), the resin-embedded portion 2 of the hollow fiber membrane of FIG. 2 does not swell like the resin-embedded portion 2 of the hollow fiber membrane, and the cut surface 5 of the hollow fiber membrane of FIG. 3 is in a state of being enlarged in a tapered shape from the cut surface 5 of the hollow fiber membrane of FIG. Has become. The cut surface 5 of the hollow fiber membrane shown in FIG. 3 is almost the same as the cut surface 5 of the hollow fiber membrane shown in FIG. 1 (when dried by the conventional method). The reason for this is that when the cut surface 4 of the embedding resin 1 and the cut surface 5 of the resin-embedded portion 2 of the hollow fiber membrane are treated with an organic solvent solution of urea, the resin 1 is caused by the action of the organic solvent that has penetrated into the resin 1.
Is softened, and at the same time, the inner diameter of the cut surface 5 of the hollow fiber membrane is enlarged by the swelling action of the organic solvent that has penetrated into the film-thickness portion of the resin-embedded portion 2 of the hollow fiber membrane. The expanded state is maintained by the action of urea. On this occasion,
It is considered that the swelling of the film thickness part by the organic solvent hardly occurs. Subsequent irradiation treatment causes a reaction between urea and the hollow fiber membrane to form a structure in which the swelling of the thickness of the hollow fiber membrane due to wetting is suppressed, and after wetting, the inner diameter expanded to a tapered shape. It is considered that the shape is realized.

【0026】次に、実施例及び比較例によって、本発明
をさらに説明する。なお、実施例と比較例に記載する諸
数値は、以下の手順にしたがって測定した。
The present invention will be further described with reference to Examples and Comparative Examples. In addition, various numerical values described in Examples and Comparative Examples were measured according to the following procedures.

【0027】<ポリウレタン樹脂包埋部切断面における
中空糸膜内径の測定>中空糸膜束を本体ケースに収納し
た後、該中空糸膜束の両端をポリウレタン樹脂で本体ケ
ースに包埋した後、該ケースの端部を切断し、中空糸膜
の少なくとも片端を開口させた。当該切断面における中
空糸膜内径を尿素処理前後及び照射処理後の各々につい
て、デジタルHDマイクロスコープVH7000(株式
会社キーエンス製)で観察、計測した。 <残血性の評価>中空糸膜型血液処理装置を以下の条件
で、その残血性を比較評価した。各血液処理装置を1.
5Lの生理食塩水で洗浄した後、牛新鮮血(ヘマトクリ
ット45%、総蛋白質濃度9.0g/dL、ヘバリン添
加量3000IU/L)を膜間圧力差100mmHg、
血液流量200mL/分の条件で3時間循環させた。各
血液処理装置あたりに1.5Lの血液を各々使用した。
その後、200mLの生理食塩水で返血操作を行った。
返血操作後、外観から、残血中空糸本数及び中空糸固定
樹脂切断面の状態を肉眼観察した。
<Measurement of Inner Diameter of Hollow Fiber Membrane at Cut Surface of Polyurethane Resin Embedding Section> After housing the hollow fiber membrane bundle in the main body case, and embedding both ends of the hollow fiber membrane bundle in the main body case with polyurethane resin, The end of the case was cut to open at least one end of the hollow fiber membrane. The hollow fiber membrane inner diameter on the cut surface was observed and measured with a digital HD microscope VH7000 (manufactured by Keyence Corporation) before and after the urea treatment and after the irradiation treatment. <Evaluation of residual blood property> The hollow fiber membrane blood treatment apparatus was comparatively evaluated for its residual blood property under the following conditions. Each blood processing device is 1.
After washing with 5 L of physiological saline, fresh blood of bovine (hematocrit 45%, total protein concentration 9.0 g / dL, hevalin added amount 3000 IU / L) was applied, and the transmembrane pressure difference was 100 mmHg.
The blood was circulated for 3 hours at a flow rate of 200 mL / min. 1.5 L of blood was used for each blood processing apparatus.
Then, the blood return operation was performed with 200 mL of physiological saline.
After the blood returning operation, from the appearance, the number of residual blood hollow fibers and the state of the cut surface of the hollow fiber-fixed resin were visually observed.

【0028】[0028]

【実施例1】中空糸膜内径180μmの血液透析用再生
セルロース中空糸膜束を本体ケースに収納して、ポリウ
レタン樹脂でケースに包埋固定した後、ポリウレタン面
を刃物で切断し、切断面の中空糸膜の両端を開口状態に
した。シャーレに入れた15%の尿素のメタノール溶液
10mLに該切断面の両面を浸漬し、中空糸膜の膜厚部
に尿素のメタノール溶液を含浸させた。付着溶液を手で
振って液切りした後、紫外線ランプEUV200GS−
4(セン特殊光源株式会社製)の管表面より下部5cm
の距離に上記含浸面を固定し、30分間照射した。その
後、他端にも同様な照射処理を実施した。その後、該本
体ケースに血液を導入用ヘッダー、導出用ヘッダーを取
り付け、残留溶媒、遊離尿素等を清浄な流水で水洗除去
し、抗酸化剤を含む注射用蒸留水を充填した後、ガンマ
線で滅菌処理することにより、有効膜面積1.5m2
中空糸膜型血液処理装置を作成し、残血性を評価した。
評価結果を表1に示す。照射面と等距離における紫外線
照射強度は、7.6mW/cm2 であった。また、滅菌
処理後のポリウレタン切断面における中空糸膜開口部の
内径を測定した結果、Dw/Ddは1.05であり、内
径の縮小化が抑制されていることが確認された。
[Example 1] A regenerated cellulose hollow fiber membrane bundle for hemodialysis having an inner diameter of 180 µm was housed in a main body case, embedded and fixed in a case with a polyurethane resin, and then the polyurethane surface was cut with a knife to cut the cut surface. Both ends of the hollow fiber membrane were opened. Both sides of the cut surface were immersed in 10 mL of 15% urea methanol solution placed in a petri dish to impregnate the membrane part of the hollow fiber membrane with the urea methanol solution. After shaking the adhering solution by hand to drain it, UV lamp EUV200GS-
5 cm below the surface of 4 (Sen Special Light Source Co., Ltd.)
The above impregnated surface was fixed at a distance of, and irradiation was performed for 30 minutes. Then, the same irradiation treatment was performed on the other end. After that, a header for introducing blood and a header for extracting blood were attached to the main body case, residual solvents, free urea, etc. were washed away with clean running water, and distilled water for injection containing an antioxidant was filled, followed by sterilization with gamma rays. A hollow fiber membrane-type blood treatment device having an effective membrane area of 1.5 m 2 was prepared by the treatment, and the residual blood property was evaluated.
The evaluation results are shown in Table 1. The ultraviolet irradiation intensity at the same distance as the irradiation surface was 7.6 mW / cm 2 . In addition, as a result of measuring the inner diameter of the hollow fiber membrane opening on the cut surface of the polyurethane after the sterilization treatment, Dw / Dd was 1.05, and it was confirmed that the reduction of the inner diameter was suppressed.

【0029】[0029]

【実施例2】中空糸膜内径を200μm、尿素濃度を1
0%にし、かつ、紫外線の照射時間を15分に変更した
以外は、実施例1と同じ方法で、セルロース中空糸膜型
血液処理装置を作成し、残血性を評価した。また、中空
糸膜開口部の内径を測定した結果、Dw/Ddは1.0
2であり、内径の縮小化が抑制されていることが確認さ
れた。その評価結果を表1に示す。
Example 2 Hollow fiber membrane inner diameter 200 μm, urea concentration 1
A cellulosic hollow fiber membrane blood treatment apparatus was prepared and the residual blood property was evaluated by the same method as in Example 1 except that the UV irradiation time was changed to 0% and the irradiation time with ultraviolet rays was changed to 15 minutes. Moreover, as a result of measuring the inner diameter of the hollow fiber membrane opening, Dw / Dd is 1.0
It was 2 and it was confirmed that the reduction of the inner diameter was suppressed. The evaluation results are shown in Table 1.

【0030】[0030]

【比較例1】尿素溶液処理及び照射固定化処理をしない
状態で、実施例1と同様にして再生セルロース中空糸膜
束を使用した血液処理装置を組み立て、実施例1と同じ
条件で水洗、滅菌処理を行って、有効膜面積1.5m2
の比較用血液処理装置を作成した。その評価結果を表1
に示す。
Comparative Example 1 A blood treatment apparatus using a regenerated cellulose hollow fiber membrane bundle was assembled in the same manner as in Example 1 without the urea solution treatment and the irradiation immobilization treatment, and washed and sterilized under the same conditions as in Example 1. After processing, effective membrane area 1.5m 2
A blood processing apparatus for comparison was prepared. The evaluation results are shown in Table 1.
Shown in.

【0031】[0031]

【比較例2】尿素溶液による含浸処理のみを行った以外
は、比較例1と同じ条件で、セルロース中空糸膜束を使
用した血液処理装置を作成した。評価結果を表1に示
す。
[Comparative Example 2] A blood treatment apparatus using a cellulose hollow fiber membrane bundle was prepared under the same conditions as in Comparative Example 1 except that only the impregnation treatment with a urea solution was performed. The evaluation results are shown in Table 1.

【0032】[0032]

【実施例3】尿素の1、5、10及び20%メタノール
溶液を使用した以外は、実施例1に示した方法と同一の
条件で各々の濃度の尿素溶液処理をした後、照射処理し
て、血液処理装置を作成した。その残血性及び中空糸膜
のDw/Ddの評価結果を表2に示す。
Example 3 A urea solution of each concentration was treated under the same conditions as in Example 1 except that 1, 5, 10 and 20% urea methanol solutions were used, followed by irradiation treatment. , Created a blood processing device. Table 2 shows the evaluation results of the residual blood property and the Dw / Dd of the hollow fiber membrane.

【0033】[0033]

【比較例4】尿素の0.1%メタノール溶液を使用した
以外は、実施例1に示した方法と同一の条件で血液処理
装置を作成した。その残血性及び中空糸膜のDw/Dd
の評価結果を表2に示す。
Comparative Example 4 A blood processing apparatus was prepared under the same conditions as the method shown in Example 1 except that a 0.1% methanol solution of urea was used. Its residual blood property and Dw / Dd of hollow fiber membrane
The evaluation results of are shown in Table 2.

【0034】[0034]

【表1】 ──────────────────────────────────── 血液処理 中空糸膜 残血中空 切断面観察結果 切断面における 装置 の素材 糸膜本数 (両切断面) 中空糸膜内径の (本) Dw/Ddの比 ──────────────────────────────────── 実施例1の装置 再生セル 6 微小な血液凝集 1.05 ロース 塊数個あり ──────────────────────────────────── 実施例2の装置 再生セル 8 微小な血液凝集 1.02 ロース 塊数個あり ──────────────────────────────────── 比較例1の装置 再生セル 約100 血液凝集塊多数 0.9 ロース あり ──────────────────────────────────── 比較例2の装置 再生セル 約100 血液凝集塊多数 0.92 ロース あり ──────────────────────────────────── 比較例3の装置 再生セル 約100 血液凝集塊多数 0.91 ロース あり ────────────────────────────────────[Table 1] ────────────────────────────────────   Blood treatment Hollow fiber membrane Residual blood hollow Observation result of cut surface   Material of the device Number of fiber membranes (both cut surfaces)                                 (Book) Dw / Dd ratio ──────────────────────────────────── Device of Example 1 Regeneration cell 6 Micro blood aggregation 1.05                   There are several loins ──────────────────────────────────── Device of Example 2 Regeneration cell 8 Micro blood aggregation 1.02                   There are several loins ──────────────────────────────────── Apparatus of Comparative Example 1 Regeneration cell Approximately 100 Blood clots are numerous 0.9                   There is loin ──────────────────────────────────── Apparatus of Comparative Example 2 Regeneration cell Approximately 100 Blood clots are numerous 0.92                   There is loin ──────────────────────────────────── Apparatus of Comparative Example 3 Regeneration cell Approximately 100 Blood clots are numerous 0.91                   There is loin ────────────────────────────────────

【0035】[0035]

【表2】 ──────────────────────────────────── 尿素溶液 中空糸膜 残血中空 切断面観察結果 切断面における 濃度 の素材 糸膜本数 (両切断面) 中空糸膜内径の (本) Dw/Ddの比 ──────────────────────────────────── 0.1% 再生セル 約80 血液凝集塊多数 0.93 (比較例4) ロース あり ──────────────────────────────────── 1% 再生セル 10 微小な血液凝集 1.02 (実施例3) ロース 塊数個あり ──────────────────────────────────── 5% 再生セル 5 微小な血液凝集 1.03 (実施例3) ロース 塊数個あり ──────────────────────────────────── 10% 再生セル 5 微小な血液凝集 1.05 (実施例3) ロース 塊数個あり ──────────────────────────────────── 20% 再生セル 10 微小な血液凝集 1.02 (実施例3) ロース 数個あり ────────────────────────────────────[Table 2] ────────────────────────────────────   Urea solution Hollow fiber membrane Residual blood hollow Observation result of cut surface   Concentration material Number of fiber membranes (both cut surfaces)                                 (Book) Dw / Dd ratio ────────────────────────────────────   0.1% Regeneration cell About 80 Many blood clots 0.93 (Comparative Example 4) With loin ────────────────────────────────────     1% Regeneration cell 10 Micro blood aggregation 1.02 (Example 3) Loin There are several lumps ────────────────────────────────────     5% Regeneration cell 5 Micro blood coagulation 1.03 (Example 3) Loin There are several lumps ────────────────────────────────────   10% Regeneration cell 5 Micro blood aggregation 1.05 (Example 3) Loin There are several lumps ────────────────────────────────────   20% Regeneration cell 10 Micro blood coagulation 1.02 (Example 3) There are several loins ────────────────────────────────────

【0036】<上記各実施例の結果の所見>表1から、
中空糸膜の樹脂包埋部の切断面に尿素溶液で処理して尿
素を含浸させた後さらに照射固定処理をした中空糸膜束
を内蔵する血液処理装置は、同じ再生セルロースの素材
の中空糸膜であっても、また、尿素処理のみを済ませた
装置や照射処理のみを済ませた装置に比べても、残血特
性がきわめて改善されることが理解できる。表2から、
中空糸膜の樹脂包埋部の切断面を1〜20%濃度の尿素
溶液で処理して尿素を含浸させた後さらに照射固定処理
をした中空糸膜束を内蔵する血液処理装置は、同じ再生
セルロースの素材の中空糸膜であっても、0.1%濃度
の尿素溶液処理の装置に比べて、残血特性がきわめて改
善されることが理解できる。
<Observation of Results of Each Example> From Table 1,
A blood treatment device that incorporates a hollow fiber membrane bundle that has been treated with a urea solution on the cut surface of the resin-embedded portion of the hollow fiber membrane to impregnate it with urea and then fixed by irradiation is a hollow fiber made of the same regenerated cellulose material. It can be understood that the residual blood characteristics are significantly improved even when the membrane is used, or when compared with a device that has undergone only urea treatment or a device that has only undergone irradiation treatment. From Table 2,
The blood treatment device incorporating the hollow fiber membrane bundle, which is obtained by treating the cut surface of the resin-embedded portion of the hollow fiber membrane with a urea solution having a concentration of 1 to 20% to impregnate urea, and then further performing irradiation fixing treatment, has the same regeneration. It can be understood that even with a hollow fiber membrane made of a cellulose material, the residual blood characteristics are significantly improved as compared with a device for treating a 0.1% concentration urea solution.

【0037】[0037]

【発明の効果】以上、詳細に説明するとおり、本発明
は、セルロース系中空糸膜からなる血液処理装置の中空
糸膜の血液導入部及び血液導出部の切断面における中空
糸膜の湿潤による内径縮小を抑制することができるの
で、血液処理装置の血液流動抵抗を大きく改善できる。
したがって、本発明の中空糸膜型血液処理装置は、血液
の流動時の活性化を抑制し、使用後の血液処理装置内に
残留する血液量、すなわち残血量を減少させた、すぐれ
た残血特性を有する血液処理装置である。したがって、
本発明により、残血が少ないので、血液透析、血液濾
過、血液透析濾過等に好適に使用できる中空糸膜型血液
処理装置とその製造方法を提供できる。
As described above in detail, according to the present invention, the inner diameter of the hollow fiber membrane of the blood treatment apparatus comprising the cellulosic hollow fiber membrane is wetted by the wetting of the hollow fiber membrane at the cut surface of the blood introducing section and the blood introducing section of the hollow fiber membrane. Since the reduction can be suppressed, the blood flow resistance of the blood processing apparatus can be greatly improved.
Therefore, the hollow fiber membrane-based blood processing apparatus of the present invention suppresses activation during blood flow and reduces the amount of blood remaining in the blood processing apparatus after use, that is, the amount of residual blood. A blood processing apparatus having blood characteristics. Therefore,
INDUSTRIAL APPLICABILITY The present invention can provide a hollow fiber membrane-type blood treatment apparatus and a method for producing the same, which has less residual blood and can be suitably used for hemodialysis, hemofiltration, hemodiafiltration, and the like.

【図面の簡単な説明】[Brief description of drawings]

【図1】従来の血液処理装置用中空糸膜とそれを包埋固
定する樹脂の乾燥状態における切断面の説明図
FIG. 1 is an explanatory view of a cut surface of a conventional hollow fiber membrane for a blood processing apparatus and a resin for embedding and fixing the hollow fiber membrane in a dry state.

【図2】従来の血液処理装置用中空糸膜とそれを包埋固
定する樹脂の湿潤状態における切断面の説明図
FIG. 2 is an explanatory view of a cut surface in a wet state of a conventional hollow fiber membrane for a blood processing apparatus and a resin for embedding and fixing the hollow fiber membrane.

【図3】本発明の血液処理装置用中空糸膜とそれを包埋
固定する樹脂の湿潤状態における切断面の説明図
FIG. 3 is an explanatory view of a cut surface of a hollow fiber membrane for a blood processing apparatus of the present invention and a resin for embedding and fixing the hollow fiber membrane in a wet state.

【符号の説明】[Explanation of symbols]

1:中空糸膜を包埋固定する樹脂 2:中空糸膜の樹脂包埋部 3:中空糸膜の非樹脂包埋部 4:包埋固定樹脂の切断面 5:中空糸膜の樹脂包埋部の切断面 1: Resin for embedding and fixing hollow fiber membranes 2: Resin embedding part of hollow fiber membrane 3: Non-resin embedded part of hollow fiber membrane 4: Cut surface of embedded fixing resin 5: Cut surface of the resin-embedded portion of the hollow fiber membrane

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4C058 AA12 BB06 KK02 4C077 AA05 BB01 CC06 EE01 EE03 GG05 KK11 LL05 NN03 PP03 PP14    ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4C058 AA12 BB06 KK02                 4C077 AA05 BB01 CC06 EE01 EE03                       GG05 KK11 LL05 NN03 PP03                       PP14

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 中空糸膜束の端部を樹脂で包埋固定して
樹脂包埋部を形成してあるセルロース系中空糸膜束を内
蔵し、少なくとも一方の樹脂包埋部の端部を切断して中
空糸膜を開口させてあると共に、該中空糸膜の樹脂包埋
部の切断面を尿素の有機溶媒溶液で処理して尿素を含浸
させてあり、かつ、照射処理をしてあることを特徴とす
る中空糸膜型血液処理装置。
1. A cellulosic hollow fiber membrane bundle in which an end portion of a hollow fiber membrane bundle is embedded and fixed in a resin to form a resin-embedded portion, and at least one end portion of the resin-embedded portion is provided. The hollow fiber membrane is cut to open the hollow fiber membrane, the cut surface of the resin-embedded portion of the hollow fiber membrane is treated with an organic solvent solution of urea to be impregnated with urea, and irradiation treatment is performed. A hollow fiber membrane-type blood treatment device characterized by the above.
【請求項2】 セルロース系中空糸膜束の素材が、再生
セルロースである請求項1に記載の中空糸膜型血液処理
装置。
2. The hollow fiber membrane-type blood treatment apparatus according to claim 1, wherein the material of the cellulosic hollow fiber membrane bundle is regenerated cellulose.
【請求項3】 中空糸を包埋固定する樹脂が、ポリウレ
タン樹脂である請求項1又は2に記載の中空糸膜型血液
処理装置。
3. The hollow fiber membrane-type blood treatment device according to claim 1, wherein the resin for embedding and fixing the hollow fiber is a polyurethane resin.
【請求項4】 樹脂包埋部の切断面における中空糸膜の
開口部の乾燥時と湿潤時の内径比が以下の範囲である請
求項1から3のいずれかに記載の中空糸膜型血液処理装
置。 Dw/Dd=1.0〜1.1 ここで、Dwは、樹脂包埋部切断面における水湿潤状態
の中空糸の内径を、Ddは、水湿潤状態前の乾燥状態
での中空糸膜の内径を示す。
4. The hollow fiber membrane blood according to claim 1, wherein an inner diameter ratio of the opening of the hollow fiber membrane on the cut surface of the resin-embedded portion when the opening is dry and when the opening is wet is within the following range. Processing equipment. Dw / Dd = 1.0 to 1.1 Here, Dw is the inner diameter of the hollow fiber membrane in the water-wet state on the cut surface of the resin-embedded portion, and Dd is the hollow fiber membrane in the dry state before the water-wet state. Indicates the inner diameter of.
【請求項5】 中空糸膜束の端部を樹脂で包埋固定して
樹脂包埋部を形成してあるセルロース系中空糸膜束を内
蔵し、少なくとも一方の樹脂包埋部の端部を切断して中
空糸膜を開口させると共に、該中空糸膜の樹脂包埋部の
切断面を尿素の有機溶媒溶液で処理して尿素を含浸させ
た後、照射処理することを特徴とする中空糸膜型血液処
理装置の製造方法。
5. A cellulosic hollow fiber membrane bundle in which an end portion of a hollow fiber membrane bundle is embedded and fixed with a resin to form a resin embedding portion is built in, and at least one end portion of the resin embedding portion is provided. A hollow fiber which is cut to open the hollow fiber membrane, and the cut surface of the resin-embedded portion of the hollow fiber membrane is treated with an organic solvent solution of urea to impregnate urea and then subjected to irradiation treatment. Membrane-type blood processing apparatus manufacturing method.
【請求項6】 尿素の有機溶媒溶液が、メタノール溶液
である請求項5に記載の中空糸膜型血液処理装置の製造
方法。
6. The method for producing a hollow fiber membrane blood treatment apparatus according to claim 5, wherein the organic solvent solution of urea is a methanol solution.
【請求項7】 尿素溶液の濃度が、1〜20重量%であ
る請求項5又は6に記載の中空糸膜型血液処理装置の製
造方法。
7. The method for producing a hollow fiber membrane-based blood treatment device according to claim 5, wherein the urea solution has a concentration of 1 to 20% by weight.
【請求項8】 照射処理として、紫外線照射をすること
とした請求項5から7のいずれかに記載の中空糸膜型血
液処理装置の製造方法。
8. The method for manufacturing a hollow fiber membrane-type blood treatment device according to claim 5, wherein the irradiation treatment is irradiation with ultraviolet rays.
JP2002047285A 2002-02-25 2002-02-25 Blood processing device of hollow fiber membrane type and manufacturing method therefor Pending JP2003245346A (en)

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Publication Number Publication Date
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ID=28660387

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017035644A (en) * 2015-08-06 2017-02-16 旭化成メディカル株式会社 Hollow fiber membrane module and production method of the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017035644A (en) * 2015-08-06 2017-02-16 旭化成メディカル株式会社 Hollow fiber membrane module and production method of the same

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