JPH0613737Y2 - Hemodialyzer - Google Patents

Hemodialyzer

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Publication number
JPH0613737Y2
JPH0613737Y2 JP2281989U JP2281989U JPH0613737Y2 JP H0613737 Y2 JPH0613737 Y2 JP H0613737Y2 JP 2281989 U JP2281989 U JP 2281989U JP 2281989 U JP2281989 U JP 2281989U JP H0613737 Y2 JPH0613737 Y2 JP H0613737Y2
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JP
Japan
Prior art keywords
dialysate
blood
purification chamber
membrane
hemodialyzer
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.)
Expired - Lifetime
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JP2281989U
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Japanese (ja)
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JPH02114054U (en
Inventor
征二 山上
利明 増田
Original Assignee
株式会社ニッショー
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Priority to JP2281989U priority Critical patent/JPH0613737Y2/en
Publication of JPH02114054U publication Critical patent/JPH02114054U/ja
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Publication of JPH0613737Y2 publication Critical patent/JPH0613737Y2/en
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Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は血液透析器に関し、詳しくは透析液中に含有す
る細菌、エンドトキシン等を除去する透析液濾過膜が仕
切部材を介して半透膜と筒内に一体に収容されてなる血
液透析器に関する。
[Detailed Description of the Invention] [Industrial application] The present invention relates to a hemodialyzer, and more specifically, a dialysate filter membrane for removing bacteria, endotoxin, etc. contained in a dialysate is a semipermeable membrane through a partition member. And a hemodialyzer integrally housed in a cylinder.

〔従来の技術〕[Conventional technology]

腎臓機能不全の患者の治療や生命の維持に血液を透析す
る透析療法は既に確立され広く使用されている。また膜
機能の向上により患者の体液中に蓄積した尿素、尿酸等
の透析、除去だけでなく、毛根管症候群等を防止するた
めに、β−マイクログロブリンなどの中分子量物質の
除去にも使用範囲が広がりつつある。しかしながら、そ
の反面、透析膜の高機能化に伴い、当初予想もしなかっ
た合併症や概念の異なった疾患の発生を見るにいたって
いる。
Dialysis therapy for dialysis of blood to treat patients with renal insufficiency and to maintain life is already established and widely used. In addition to dialysis and removal of urea, uric acid, etc. accumulated in body fluids of patients due to improvement of membrane function, in addition to removal of medium molecular weight substances such as β 2 -microglobulin to prevent hair root canal syndrome etc. The range of use is expanding. However, on the other hand, as the dialysis membrane becomes highly functional, the occurrence of unforeseen complications and diseases with different concepts has been observed.

〔考案が解決しようとする課題〕 例えば、水道水中の弗素化合物が原因でないかといわれ
ている骨軟化症、硬水度の高い水を使用して透析を行っ
た際起こる高カルシウム血症、上水道の殺菌に使用する
クロールがアンモニアと反応して生成するクロラミンが
原因でないかといわれている貧血症、エンドドキシンに
よる発熱、あるいはその他細菌が血中の抗体と凝集反応
を起こして生じる合併症候群が起きることが知られてい
る。特に、エンドトキシンはある種の界面活性物質の存
在下では、サブユニットに解離し半透膜の微細孔を通過
することがあり、その解決が要望されてきた。
[Problems to be solved by the invention] For example, osteomalacia, which is said to be caused by a fluorine compound in tap water, hypercalcemia that occurs when dialysis is performed using highly hard water, and sterilization of water supply. It is known that an anemia, which is said to be caused by chloramine produced by the reaction of chlor with ammonia, a fever due to endotoxin, or a complication syndrome caused by other bacteria causing an agglutination reaction with antibodies in the blood. ing. In particular, endotoxin may be dissociated into subunits and pass through the micropores of the semipermeable membrane in the presence of a certain kind of surface-active substance, and its solution has been demanded.

〔課題を解決するための手段〕[Means for Solving the Problems]

本考案者等はこれらの要望に応えんために鋭意検討した
結果、かかる症状が透析液中に含まれている細菌やエン
ドトキシンが透析中に半透膜の微細孔から血液中に侵入
することが原因であることを見出し本考案に到達した。
すなわち、本考案は、筒内に収容された中空繊維半透膜
を介して、血液を透析液と接触せしめることにより、該
血液を浄化させる血液透析器において、血液導入口およ
び血液導出口と、透析液導入口および透析液導出口と、
筒内に半透膜の孔径が0.001〜0.05μの中空繊維半透膜
が収容されてなる血液浄化室と濾過膜の孔径が0.5μ以
下の透析液濾過膜が収容されてなる透析液浄化室とに区
分する長手方向に延びてなる仕切部材と、前記透析液浄
化室で清浄化された透析液を前記血液浄化室へ流入せし
める前記仕切部材に設けられた清浄透析液流入口とから
なる血液透析器である。
As a result of diligent studies conducted by the present inventors in order to meet these demands, it has been found that bacteria and endotoxin contained in the dialysate enter the blood through the micropores of the semipermeable membrane during dialysis. We found that it was the cause and arrived at the present invention.
That is, the present invention is a hemodialyzer that purifies blood by bringing blood into contact with a dialysate through a hollow fiber semipermeable membrane housed in a cylinder, and a blood inlet and a blood outlet. Dialysate inlet and dialysate outlet,
A blood purification chamber containing a hollow fiber semipermeable membrane with a semipermeable membrane having a pore size of 0.001 to 0.05 μ and a dialysate purification chamber having a dialysate filtration membrane with a filtration membrane having a pore size of 0.5 μ or less. Blood composed of a partitioning member extending in the longitudinal direction that is divided into and a clean dialysate inlet provided in the partitioning member that allows the dialysate purified in the dialysate purification chamber to flow into the blood purification chamber. It is a dialyzer.

〔作用〕[Action]

本考案血液透析器はかかる構成からなっているので、透
析液中に存在した細菌やエンドトキシンは透析液濾過膜
で除去されて、患者の血液と半透膜を介して接触するこ
とができる。そして半透膜の血液導出口付近で透析液側
の圧力が血液側の圧力より高くなり、透析液が半透膜の
微細孔から血液中へ侵入する事態が生じても、細菌やエ
ンドトキシンが除去された透析液であるので、細菌等が
原因で起こる種々の症状は回避することができる。
Since the hemodialyzer of the present invention has such a structure, the bacteria and endotoxins present in the dialysate can be removed by the dialysate filter membrane and contact the patient's blood through the semipermeable membrane. Even if the pressure on the dialysate side becomes higher than the pressure on the blood side near the blood outlet of the semipermeable membrane and the dialysate enters the blood through the micropores of the semipermeable membrane, bacteria and endotoxins are removed. Since it is a dialyzed solution, various symptoms caused by bacteria and the like can be avoided.

〔実施例〕〔Example〕

次に、本考案血液透析器の一実施例を図面に基づいて説
明する。
Next, an embodiment of the hemodialyzer of the present invention will be described with reference to the drawings.

第1図は半透膜および透析液濾過膜として多孔性中空繊
維を使用してなる血液透析器の断面図である。
FIG. 1 is a sectional view of a hemodialyzer using porous hollow fibers as a semipermeable membrane and a dialysate filtration membrane.

図中1は血液導入口、2は血液導出口、3は透析液導入
口、4は透析液導出口、5は仕切部材、6は中空繊維
(半透膜)、7は中空繊維(透析液濾過膜)8〜10は密
封部材、11は清浄化透析液貯留室、12は清浄化透析液流
入口、13は外筒、14は血液浄化室、15は透析液浄化室を
示す。
In the figure, 1 is a blood inlet, 2 is a blood outlet, 3 is a dialysate inlet, 4 is a dialysate outlet, 5 is a partition member, 6 is a hollow fiber (semipermeable membrane), 7 is a hollow fiber (dialysate). Filtration membranes 8 to 10 are sealing members, 11 is a purified dialysate storage chamber, 12 is a purified dialysate inlet, 13 is an outer cylinder, 14 is a blood purification chamber, and 15 is a dialysate purification chamber.

第1図は血液透析器は長手方向に延びた円筒形の外筒13
内に、仕切部材5によって区分された血液浄化室14と透
析液浄化室15とから成っている。そして外筒13の上端に
は血液導入口1、下端には血液導出口2、外筒13の上部
側端には透析液導入口3および上部側端の他の位置には
透析液導出口4が具備されて開口してなっている。該開
口部はプラスチックチューブなどと連結して血液または
透析液の導入または導出を行う。
FIG. 1 shows a hemodialyzer having a cylindrical outer cylinder 13 extending in the longitudinal direction.
It is composed of a blood purification chamber 14 and a dialysate purification chamber 15 which are divided by a partition member 5. The outer cylinder 13 has a blood inlet 1 at the upper end, a blood outlet 2 at the lower end, a dialysate inlet 3 at the upper end of the outer cylinder 13, and a dialysate outlet 4 at other positions of the upper end. It is equipped with and is opened. The opening is connected to a plastic tube or the like to introduce or withdraw blood or dialysate.

透析液浄化室15は多数本の多孔性中空繊維が外筒13の長
手方向にほぼ平行に配列しており、該繊維の上端は密封
部材8によって中空部が封鎖されており、繊維の下端は
密封部材10を通り抜け中空部が清浄化透析液貯留室11に
開口した構造をしている。
In the dialysate purification chamber 15, a large number of porous hollow fibers are arranged substantially parallel to the longitudinal direction of the outer cylinder 13, the upper end of the fibers is closed by the sealing member 8 at the hollow part, and the lower end of the fibers is A hollow portion passing through the sealing member 10 is opened to the purified dialysate storage chamber 11.

清浄化透析液貯留室11は仕切部材9および血液浄化室14
の多孔性中空繊維6の下端を密封する密封部材9と、前
記密封部材10と外筒の内壁および仕切部材5からなって
おり、仕切部材5に設けられた開口、すなわち清浄化透
析液流入口12から前記貯留室11に貯留された清浄化透析
液が血液浄化室14へ流入するようになっている。
The purified dialysate storage chamber 11 includes the partition member 9 and the blood purification chamber 14.
The sealing member 9 for sealing the lower end of the porous hollow fiber 6, the sealing member 10, the inner wall of the outer cylinder, and the partition member 5, and the opening provided in the partition member 5, that is, the purified dialysate inlet port. The purified dialysate stored in the storage chamber 11 from 12 flows into the blood purification chamber 14.

該血液浄化室14は多数本の多孔性中空繊維6が外筒13の
長手方向にほぼ平行に配列しており、その上端および下
端は密封部材8および9によって密封されており、該繊
維の中空部は密封部材8および9を通り抜け、密封部材
の外側で開口してなっている。
In the blood purification chamber 14, a large number of porous hollow fibers 6 are arranged substantially parallel to the longitudinal direction of the outer cylinder 13, and the upper and lower ends thereof are sealed by sealing members 8 and 9, and the hollow fibers are hollow. The part passes through the sealing members 8 and 9 and opens outside the sealing member.

血液導入口1から供給された患者の血液は多孔性中空繊
維6の中空部を通過する過程で、該中空繊維を構成する
半透膜を介して、清浄化透析液流入口12から流入した清
浄化透析液と接触して透析を行い、清浄化血液として血
液導出口2からチューブ、ポンプ等によって患者に返血
される。
The blood of the patient supplied from the blood inlet 1 passes through the hollow portion of the porous hollow fiber 6 and passes through the semipermeable membrane that constitutes the hollow fiber, and flows from the cleaning dialysate inlet 12 through the cleaning dialysate 12. Dialysis is carried out by contacting the activated dialysate, and purified blood is returned to the patient from the blood outlet 2 by a tube, a pump or the like.

第1図では血液浄化室14の半透膜は多孔性中空繊維から
なっているが、シート状、管状の半透膜を用いてプレー
ト型、コイル型として使用することも可能である。
In FIG. 1, the semipermeable membrane of the blood purification chamber 14 is made of porous hollow fiber, but it is also possible to use a sheet-shaped or tubular semipermeable membrane as a plate type or a coil type.

半透膜の材料としては、再生セルロース、酢酸セルロー
ス、ポリビニルアルコール、ポリオレフィン、ポリスル
ホン、ポリアクリルニトリル、ポリメチルメタクリレー
トなどが使用される。
As the material of the semipermeable membrane, regenerated cellulose, cellulose acetate, polyvinyl alcohol, polyolefin, polysulfone, polyacrylonitrile, polymethylmethacrylate, etc. are used.

血液浄化室14で使用する半透膜の孔径は0.001〜0.05
μ、好ましくは0.005〜0.1μである。孔径が0.001μ未
満であると、透析効率が減少する傾向があり、孔径が0.
05μを超えるとアルブミン等の有効な蛋白質も除去され
る傾向がある。
The pore size of the semipermeable membrane used in the blood purification chamber 14 is 0.001 to 0.05.
μ, preferably 0.005 to 0.1 μ. If the pore size is less than 0.001μ, the dialysis efficiency tends to decrease, and the pore size is 0.
If it exceeds 05μ, effective proteins such as albumin tend to be removed.

第1図の血液浄化室14において、多数本の中空繊維6は
両端で密封部材8および9により固定されているが、密
封部材の材料としては、エポキシ樹脂、ポリウレタン樹
脂、シリコン樹脂等が挙げられる。
In the blood purification chamber 14 of FIG. 1, a large number of hollow fibers 6 are fixed at both ends by sealing members 8 and 9, and examples of the material of the sealing member include epoxy resin, polyurethane resin, silicone resin and the like. .

一方、第1図において、透析液浄化室15の透析液濾過膜
7は多孔性中空繊維からなっているが、シート状、管状
の微細多孔性膜を用いてプレート型、コイル型として使
用することも可能である。透析液濾過膜材料としては、
ポリアミド、ポリエステテル、ポリビニルアルコール、
ポリカーボネート、ポリオレフィン、ポリスルホン、ポ
リアクリレートなどが使用され、特にポリエチレンまた
はポリプロピレンからなるエンドトキシン吸着性の膜が
好ましい。
On the other hand, in FIG. 1, the dialysate filtration membrane 7 in the dialysate purification chamber 15 is made of porous hollow fiber, but it should be used as a plate type or a coil type by using a sheet-shaped or tubular microporous membrane. Is also possible. As a dialysate filtration membrane material,
Polyamide, polyester, polyvinyl alcohol,
Polycarbonate, polyolefin, polysulfone, polyacrylate, etc. are used, and an endotoxin-adsorptive membrane made of polyethylene or polypropylene is particularly preferable.

透析液濾過膜7の孔径は0.5μ以下が好ましく、特に、
0.05〜1.0μが好ましい。孔径が0.5μを超えると、透析
液中に含まれている細菌が透析液濾過膜7を通過し、清
浄化透析液中に入る危険がある。
The pore diameter of the dialysate filtration membrane 7 is preferably 0.5 μ or less,
0.05 to 1.0 μ is preferable. If the pore size exceeds 0.5 μ, there is a risk that bacteria contained in the dialysate will pass through the dialysate filter membrane 7 and enter the purified dialysate.

第1図の透析液浄化室15において、透析液は透析液導入
口3から多孔性中空繊維7の外側から微細多孔性膜の微
細孔を通過して、該繊維の中空部に侵入するように構成
されているが、反対に透析液は多孔性中空繊維7の中空
部から該繊維の外側に浸出するように構成されていても
よい。
In the dialysate purification chamber 15 of FIG. 1, the dialysate should pass through the dialysate inlet 3 from the outside of the porous hollow fiber 7 through the fine pores of the microporous membrane to enter the hollow portion of the fiber. However, conversely, the dialysate may be configured to leach from the hollow portion of the porous hollow fiber 7 to the outside of the fiber.

多孔性中空繊維7の両端は密封部材8および9で固定さ
れ繊維束が外筒14の長手方向にほぼ平行に配列している
が、密封部材10の材料としては、エポキシ樹脂、ポリウ
レタン樹脂、シリコン樹脂等が挙げられる。
Both ends of the porous hollow fiber 7 are fixed by sealing members 8 and 9, and the fiber bundles are arranged substantially parallel to the longitudinal direction of the outer cylinder 14. The material of the sealing member 10 is epoxy resin, polyurethane resin, silicone. Resin etc. are mentioned.

透析液導入口3から導入された透析液は透析液濾過膜7
でエンドトキシンや細菌を除去し、該濾過膜7を通過し
た清浄化透析液は中空繊維の中空部から清浄化透析液貯
留室11に貯留される。
The dialysate introduced through the dialysate inlet 3 is the dialysate filtration membrane 7.
The endotoxin and bacteria are removed by the method, and the purified dialysate that has passed through the filtration membrane 7 is stored in the purified dialysate storage chamber 11 from the hollow portion of the hollow fiber.

次いで、該貯留室11に貯留された清浄化透析液は仕切部
材5に設けられた間隙部、すなわち清浄化透析液流入口
12から血液浄化室14へ流入し、該浄化室に収容された多
孔性中空繊維6の微細孔膜を介して、該中空繊維の中空
部を流れる血液と接触して透析を行い、透析液導出口4
から流出される。
Next, the cleaning dialysate stored in the storage chamber 11 is a gap provided in the partition member 5, that is, the cleaning dialysate inlet.
From 12 to the blood purification chamber 14, through the fine pore membrane of the porous hollow fiber 6 housed in the purification chamber, it comes into contact with the blood flowing through the hollow portion of the hollow fiber for dialysis, and the dialysate is introduced. Exit 4
Spilled from.

仕切部材5は外筒13の長手方向にほぼ平行に配置され、
血液透析器の筒内部を血液浄化室14と透析液浄化室15と
に区分し、その両端は密封部材8および10で固定されて
いる。仕切部材5の材料としてはポリオレフィン、ポリ
カーボネート、ポリアクリレート、ポリアクリルニトリ
ル・スチレン、ポリアクリルニトリル・ブタジエン・ス
チレン、ポリ塩化ビニル等が挙げられ、外筒14と同じ材
料であるのが好ましい。
The partition member 5 is arranged substantially parallel to the longitudinal direction of the outer cylinder 13,
The inside of the cylinder of the hemodialyzer is divided into a blood purification chamber 14 and a dialysate purification chamber 15, both ends of which are fixed by sealing members 8 and 10. Examples of the material of the partition member 5 include polyolefin, polycarbonate, polyacrylate, polyacrylonitrile / styrene, polyacrylonitrile / butadiene / styrene, polyvinyl chloride and the like, and the same material as the outer cylinder 14 is preferable.

以下実施例および比較例で本考案の一例を説明する。An example of the present invention will be described below with reference to Examples and Comparative Examples.

実施例1 第1図の血液透析器において、血液浄化室14は内径200
μ、外径230μ、平均孔径0.003μのセルロース中空繊維
を用い、有効膜面積1.1m2であり、透析液浄化室15はポ
リエチレン中空繊維(三菱レイヨン製ステラポアEHF-27
0T、平均短手方向孔径0.20μ)を用い、有効膜面積300c
m2で透析液の濾過を行った。
Example 1 In the hemodialyzer shown in FIG. 1, the blood purification chamber 14 has an inner diameter of 200
μ, outer diameter 230 μ, average pore size 0.003 μ cellulose hollow fiber, effective membrane area 1.1 m 2 , dialysate purification chamber 15 polyethylene hollow fiber (Mitsubishi Rayon Stellapore EHF-27
0T, mean lateral pore size 0.20μ), effective membrane area 300c
The dialysate was filtered through m 2 .

透析条件は透析液量500ml/min.、限外濾過率4.0mi/hr.m
mHgであった。36人の患者について透析を行い、エリサ
法(ELISA法)で患者血液中のエンドトキシン抗体の有
無を判定した。
The dialysis conditions are: dialysate volume 500 ml / min., Ultrafiltration rate 4.0 mi / hr.m.
It was mHg. Dialysis was performed on 36 patients, and the presence or absence of endotoxin antibody in the blood of the patients was determined by Elisa method (ELISA method).

測定法は透析液(水)より細菌を採取し、固定培養後、
フェノール法によりエンドトキシンを抽出し、それを抗
原として患者の血液と反応させ、エンドトキシン抗体の
有無を測定した。その結果を第1表に示す。
The measuring method is to collect bacteria from dialysate (water), and after fixed culture,
The endotoxin was extracted by the phenol method and reacted with the blood of the patient using it as an antigen, and the presence or absence of endotoxin antibody was measured. The results are shown in Table 1.

比較例1 第1図の血液透析器において、血液浄化室14は実施例1
で使用した半透膜を用い、透析液浄化室15は透析液濾過
膜7を取り除いてなる血液透析器を用い、実施例1と同
じ条件で透析を行った。
Comparative Example 1 In the hemodialyzer shown in FIG.
Dialysis was carried out under the same conditions as in Example 1, using the semipermeable membrane used in 1. and a hemodialyzer in which the dialysate purification chamber 15 was removed from the dialysate purification chamber 15.

このようにして透析を行った患者約50人の血液を採取
し、実施例1と同じ方法でエンドトキシン抗体の有無を
測定した。その結果を第1表に示す。
The blood of about 50 patients thus dialyzed was collected, and the presence or absence of endotoxin antibody was measured by the same method as in Example 1. The results are shown in Table 1.

実施例2 実施例1の血液透析器の血液浄化室14において、中空繊
維6として、内径200μ、外径230μ、平均孔径0.02μの
セルロース中空繊維を用い、有効濾過面積1.1m2とし、
透析液浄化室15は実施例1で使用したポリエチレン中空
繊維を用いて透析を行った。透析条件は透析液量500ml/
min.、限外濾過率20ml/hr.mmHgであった。41人の患者に
ついて実施例1と同じ方法でエンドトキシン抗体のの有
無を測定した。その結果を第1表に示す。
Example 2 In the blood purification chamber 14 of the hemodialyzer of Example 1, cellulose hollow fibers having an inner diameter of 200 μ, an outer diameter of 230 μ, and an average pore diameter of 0.02 μ were used as the hollow fibers 6, and the effective filtration area was 1.1 m 2 .
In the dialysate purification chamber 15, the polyethylene hollow fibers used in Example 1 were used for dialysis. The dialysis condition is a dialysate volume of 500 ml /
The ultrafiltration rate was 20 ml / hr.mmHg. The presence or absence of endotoxin antibody was measured in the same manner as in Example 1 in 41 patients. The results are shown in Table 1.

比較例2 第1図の血液透析器において、血液浄化室14は実施例2
で使用した半透膜を用い、透析液浄化室15は透析液濾過
膜7を取り除いてなる血液透析器を用い、実施例2と同
じ条件で透析を行った。このようにして透析を行った患
者約50人の血液を採取し、実施例1と同じ方法でエンド
トキシン抗体の有無を測定した。その結果を第1表に示
す。
Comparative Example 2 In the hemodialyzer shown in FIG.
Dialysis was carried out under the same conditions as in Example 2, using the semipermeable membrane used in 1. and the hemodialyzer in which the dialysate filtration membrane 7 was removed in the dialysate purification chamber 15. The blood of about 50 patients thus dialyzed was collected, and the presence or absence of endotoxin antibody was measured by the same method as in Example 1. The results are shown in Table 1.

比較例3 健康人の血液を採取し、実施例1と同じ方法でエンドト
キシン抗体の有無を測定した。
Comparative Example 3 Blood of a healthy person was collected, and the presence or absence of endotoxin antibody was measured by the same method as in Example 1.

第1表から明らかなように、透析液濾過膜を備えた実施
例の血液透析器で透析した患者から採取した血液のエン
ドトキシン抗体の発生率は健康人の血液から採取した比
較例3の結果とほぼ同じである。また透析液濾過膜を備
えていない比較例の血液透析器で透析した患者から採取
した血液と比較すると、実施例1および2のエンドトキ
シン抗体の発生率は低かった。
As is clear from Table 1, the incidence of endotoxin antibody in the blood collected from the patients dialyzed by the hemodialyzer of the example equipped with the dialysate filtration membrane was the same as that of Comparative Example 3 collected from the blood of healthy persons. It is almost the same. In addition, the incidence of endotoxin antibody in Examples 1 and 2 was low as compared with blood collected from a patient dialyzed with a hemodialyzer of Comparative Example not equipped with a dialysate filtration membrane.

〔効果〕〔effect〕

本考案は透析液膜が仕切部材を介して半透膜と筒内に一
体に収容されてなる血液透析器であるので、透析液中に
含まれている細菌、エンドトキシン等を予め除去して透
析することができ、細菌が血中の抗体と凝集反応を起こ
して生じる合併症候群を防止することができる。
Since the present invention is a hemodialyzer in which a dialysate membrane is integrally housed in a cylinder with a semipermeable membrane via a partition member, bacteria, endotoxin, etc. contained in the dialysate are removed in advance for dialysis. It is possible to prevent the complication syndrome caused by the bacteria causing an agglutination reaction with the antibody in the blood.

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

第1図は半透膜および透析液濾過膜として多孔性中空繊
維を使用してなる血液透析器の断面図である。 図中1は血液導入口、2は血液導出口、3は透析液導入
口、4は透析液導出口、5は仕切部材、6は中空繊維
(半透膜)、7は中空繊維(透析液濾過膜)、8〜10は
密封部材、11は清浄化透析液貯留室、12は清浄化透析液
流入口、13は外筒、14は血液浄化室、15は透析液浄化室
を示す。
FIG. 1 is a sectional view of a hemodialyzer using porous hollow fibers as a semipermeable membrane and a dialysate filtration membrane. In the figure, 1 is a blood inlet, 2 is a blood outlet, 3 is a dialysate inlet, 4 is a dialysate outlet, 5 is a partition member, 6 is a hollow fiber (semipermeable membrane), 7 is a hollow fiber (dialysate). Filtration membrane), 8 to 10 are sealing members, 11 is a purified dialysate storage chamber, 12 is a purified dialysate inlet, 13 is an outer cylinder, 14 is a blood purification chamber, and 15 is a dialysate purification chamber.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】筒内に収容された中空繊維半透膜を介し
て、血液を透析液と接触せしめることにより、該血液を
浄化させる血液透析器において、 血液導入口および血液導出口と、 透析液導入口および透析液導出口と、 筒内に半透膜の孔径が0.001〜0.05μの中空繊維半透膜
が収容されてなる血液浄化室と濾過膜の孔径が0.5μ以
下の透析液濾過膜が収容されてなる透析液浄化室とに区
分する長手方向に延びてなる仕切部材と、 前記透析液浄化室で清浄化された透析液を前記血液浄化
室へ流入せしめる前記仕切部材に設けられた清浄透析液
流入口とからなる血液透析器。
1. A hemodialyzer for purifying blood by bringing the blood into contact with a dialysate through a hollow fiber semipermeable membrane housed in a cylinder, a blood inlet and a blood outlet, and dialysis. A blood purification chamber that contains a liquid inlet and a dialysate outlet, and a hollow fiber semipermeable membrane with a semipermeable membrane with a pore size of 0.001 to 0.05μ in the cylinder, and a dialysate filter with a pore size of 0.5μ or less. A partition member extending in the longitudinal direction that is divided into a dialysate purification chamber containing a membrane, and a partition member that allows the dialysate purified in the dialysate purification chamber to flow into the blood purification chamber. A hemodialyzer comprising a clean dialysate inlet.
JP2281989U 1989-02-28 1989-02-28 Hemodialyzer Expired - Lifetime JPH0613737Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2281989U JPH0613737Y2 (en) 1989-02-28 1989-02-28 Hemodialyzer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2281989U JPH0613737Y2 (en) 1989-02-28 1989-02-28 Hemodialyzer

Publications (2)

Publication Number Publication Date
JPH02114054U JPH02114054U (en) 1990-09-12
JPH0613737Y2 true JPH0613737Y2 (en) 1994-04-13

Family

ID=31241272

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2281989U Expired - Lifetime JPH0613737Y2 (en) 1989-02-28 1989-02-28 Hemodialyzer

Country Status (1)

Country Link
JP (1) JPH0613737Y2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5218044B2 (en) * 2006-03-09 2013-06-26 東洋紡株式会社 Hollow fiber membrane excellent in performance stability, blood purifier, and method for producing hollow fiber membrane

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5218044B2 (en) * 2006-03-09 2013-06-26 東洋紡株式会社 Hollow fiber membrane excellent in performance stability, blood purifier, and method for producing hollow fiber membrane

Also Published As

Publication number Publication date
JPH02114054U (en) 1990-09-12

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