JPS6350021B2 - - Google Patents

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Publication number
JPS6350021B2
JPS6350021B2 JP57030358A JP3035882A JPS6350021B2 JP S6350021 B2 JPS6350021 B2 JP S6350021B2 JP 57030358 A JP57030358 A JP 57030358A JP 3035882 A JP3035882 A JP 3035882A JP S6350021 B2 JPS6350021 B2 JP S6350021B2
Authority
JP
Japan
Prior art keywords
adsorbent
filter
body fluid
particulate
layer
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
Application number
JP57030358A
Other languages
Japanese (ja)
Other versions
JPS58146354A (en
Inventor
Naomasa Myahara
Koichi Imai
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.)
Nikkiso Co Ltd
Original Assignee
Nikkiso 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 Nikkiso Co Ltd filed Critical Nikkiso Co Ltd
Priority to JP57030358A priority Critical patent/JPS58146354A/en
Publication of JPS58146354A publication Critical patent/JPS58146354A/en
Publication of JPS6350021B2 publication Critical patent/JPS6350021B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、血液または血液から分離された血漿
などの体液から不要もしくは毒物を吸着除去する
ための体液浄化器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a body fluid purifier for adsorbing and removing unnecessary or toxic substances from body fluids such as blood or plasma separated from blood.

〔従来の技術〕[Conventional technology]

最近、活性炭やイオン交換樹脂などの吸着剤を
血液等の潅流体液と直接接触させて体液中の有害
物質を吸着除去する体液浄化器の開発がさかんに
行なわれている。なかでも活性炭を使用したもの
は最も古くから開発が始められ、薬物中毒、肝性
昏睡の治療用として既に実用化されている。
Recently, much effort has been made to develop body fluid purifiers that adsorb and remove harmful substances from body fluids by bringing adsorbents such as activated carbon and ion exchange resins into direct contact with perfusion fluids such as blood. Among these, those using activated charcoal have been developed for the longest time, and have already been put into practical use for the treatment of drug poisoning and hepatic coma.

通常、かかる体液浄化器には吸着面積と血流と
を確保する必要性から粒径1mm程度の粒子状吸着
剤が使用され、両端部に吸着剤粒子が洩れ出ない
ようにするためのフイルターを設けた合成樹脂製
の筒状容器に充填されて用いられる。
Normally, such body fluid purifiers use particulate adsorbent with a particle size of about 1 mm to ensure adsorption area and blood flow, and filters are installed at both ends to prevent adsorbent particles from leaking out. It is used by being filled into a cylindrical container made of synthetic resin.

体外に導き出された血液は充填された吸着剤の
粒子と粒子の間隙として形成される流路を流れる
間に有害物質が吸着除去され、浄化された血液は
体内に還流されて治療が行なわれる。
The blood drawn outside the body adsorbs and removes harmful substances while flowing through channels formed by gaps between particles of the filled adsorbent, and the purified blood is returned to the body for treatment.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかし、吸着剤は、活性炭をはじめとして一般
に耐摩耗性が低く、微粉末を発生しやすいという
難点があり、体液浄化器に吸着剤を使用する場合
には、いかにして微粉末の発生を防ぎ、潅流体液
中への混入量を減少させるかが重要な問題であ
る。吸着剤微粉末が遊離すると、血流によつて体
内に運搬されて末梢血管を閉塞し、その量が多い
場合には肺、肝等の組織に沈着し、各種の障害の
原因となる。活性炭ははじめ尿毒症や薬物中毒の
治療を目的として検討が始められたが、上記の問
題点が指摘されて、広く臨床応用されるには至ら
なかつた。それが現在のように実用化されるに至
つたのは、活性炭をニトロセルロースの如き高分
子膜によつて被覆することにより微粉末の発生を
抑制するという方法が開発されて、微粉末の組織
への沈着を防止することが可能となつたためであ
る。
However, adsorbents, including activated carbon, generally have low wear resistance and are prone to generating fine powder.When using adsorbents in body fluid purifiers, how can we prevent the generation of fine powder? An important issue is how to reduce the amount of irrigant mixed into the irrigation fluid. When fine adsorbent powder is liberated, it is transported into the body by the bloodstream and occludes peripheral blood vessels, and if the amount is large, it is deposited in tissues such as the lungs and liver, causing various disorders. Activated charcoal was first studied for the purpose of treating uremia and drug addiction, but the above-mentioned problems were pointed out and it was not widely applied clinically. It came into practical use today when a method was developed to suppress the generation of fine powder by coating activated carbon with a polymer membrane such as nitrocellulose. This is because it has become possible to prevent the deposition of

しかしながら、このような方法によつて体液浄
化器からの活性炭微粉末の流出をかなりに抑制で
きるようになつたとはいうものの、使用直前に生
理的食塩水を通して洗浄することが必要であり、
この洗浄によつても活性炭微粉末の流出は皆無と
はならないので、長期にわたつて頻回の治療を行
なう必要のある慢性腎不全の治療のためには一般
的には用いられていないのが現状である。
However, although this method has made it possible to considerably suppress the flow of activated carbon fine powder from the body fluid purifier, it is still necessary to wash it with physiological saline immediately before use.
Even with this cleaning, activated carbon fine powder does not completely disappear, so it is not generally used for the treatment of chronic renal failure, which requires frequent treatment over a long period of time. This is the current situation.

また、この種の体液浄化器に対し、一般に用い
られている熱滅菌を施すと、滅菌前に比べて活性
炭微粉末の量が増加し、用途によつては使用前に
若干の洗浄が必要であることが判つた。
In addition, when this type of body fluid purifier is subjected to the commonly used heat sterilization, the amount of activated carbon fine powder increases compared to before sterilization, and depending on the application, some cleaning may be required before use. I found out something.

そこで、本発明者等は、さらに検討を加えた結
果、この活性炭微粉末の発生は、熱滅菌時に容器
が熱膨張することにより粒子状活性炭が移動して
活性炭粒子が相互にこすり合わされること、さら
にこの移動により活性炭の充填状態が弛緩し輸送
時に粒子活性炭が移動し易くなることが原因とな
つていることを知見した。
As a result of further investigation, the present inventors found that the generation of this activated carbon fine powder is due to the movement of particulate activated carbon due to thermal expansion of the container during heat sterilization, and the activated carbon particles being rubbed against each other. Furthermore, it was discovered that this movement loosens the packed state of activated carbon, making it easier for the activated carbon particles to move during transportation.

従つて、本発明の目的は、活性炭等の粒子状吸
着剤を加圧してその充填状態を密にし、予め洗浄
および滅菌を行つて組立時の吸着剤の微粉末の除
去と共に滅菌後の吸着剤微粉末の発生を防止し、
使用時に洗浄を要しない滅菌保持された体液浄化
器の製造法を提供するにある。
Therefore, an object of the present invention is to pressurize a particulate adsorbent such as activated carbon to make it densely packed, wash and sterilize it in advance, remove fine powder of the adsorbent during assembly, and remove the adsorbent after sterilization. Prevents the generation of fine powder,
To provide a method for producing a sterile body fluid purifier that does not require cleaning during use.

〔問題点を解決するための手段〕[Means for solving problems]

前記の目的を達成するため、本発明において
は、両端に入口部と出口部とを設けた筒体からな
る容器内に、活性炭等の粒子状吸着剤を充填して
吸着剤層を形成し、この吸着剤層の両側に吸着剤
の粒径より小さいメツシユ寸法のフイルタ部材を
張設して体液浄化器を構成し、 前記吸着剤層の両側に張設したフイルタ部材を
外方からそれぞれ可調整に押圧して粒子状吸着剤
を層内で移動しないように加圧保持し、次いで前
記粒子状吸着剤を洗浄して微粉末等を除去した後
ガンマー線照射による滅菌を行うことを特徴とす
る。
In order to achieve the above object, in the present invention, a particulate adsorbent such as activated carbon is filled in a cylindrical container having an inlet and an outlet at both ends to form an adsorbent layer, A body fluid purifier is constructed by extending filter members with a mesh size smaller than the particle size of the adsorbent on both sides of the adsorbent layer, and the filter members extended on both sides of the adsorbent layer can be adjusted from the outside. The particulate adsorbent is held under pressure so as not to move within the layer, and then the particulate adsorbent is washed to remove fine powder, etc., and then sterilized by gamma ray irradiation. .

〔作用〕[Effect]

本発明において、容器内のフイルタ位置が決め
られている場合には、フイルタ間の容積以上に粒
子状吸着剤を充填し、フイルタを圧力変型させた
状態で所定の位置に装填することにより、フイル
タの弾力を利用して粒子状吸着剤の層を押圧状態
に保つことができる。また、少くとも一方のフイ
ルタ位置が粒子状吸着剤の充填量に応じて任意に
粒子状吸着剤の層を押圧した状態に設定できる構
造であれば非常に便利である。さらにまた、フイ
ルタの位置を固定することなく、スプリングフイ
ルタに圧力をかけてもよい。
In the present invention, when the filter positions in the container are determined, the particulate adsorbent is filled in an amount greater than the volume between the filters, and the filters are pressure-deformed and loaded at the predetermined positions. The layer of particulate adsorbent can be kept in a compressed state by using the elasticity of the adsorbent. Further, it would be very convenient if at least one filter position could be set to a state where the layer of particulate adsorbent is pressed arbitrarily depending on the filling amount of particulate adsorbent. Furthermore, pressure may be applied to the spring filter without fixing the position of the filter.

フイルタとしては、スクリーンメツシユ不織
布、多孔板等を使用することができる。いずれも
吸着剤粒子を通過させない孔径であることが必須
である。フイルタの応力緩和を防ぐため適当な補
強を行なうのが好ましい。材質としてはガンマー
線に耐えるものであることも必須要件である。
As the filter, a screen mesh nonwoven fabric, a perforated plate, etc. can be used. In both cases, it is essential that the pores have a diameter that does not allow adsorbent particles to pass through. Appropriate reinforcement is preferably provided to prevent stress relaxation of the filter. It is also essential that the material be resistant to gamma rays.

容器の長さや断面積を充填後収縮させることに
より押圧力をかけることも可能である。
It is also possible to apply a pressing force by shrinking the length or cross-sectional area of the container after filling.

また、本発明の効果を充分得るためには、粒子
状活性炭の層を押圧する前に、粒子状活性炭の充
填状態をできるだけ密にしておくのが好ましい。
そのため一般的には円筒型でその両端に出入口を
有する充填容器をほぼ垂直にたて、その底に一方
のフイルタを装填し、容器を適当に振動しつつ粒
子状活性炭を水と共に容器上方から流し込み、余
分の水を底部のフイルタを介して抜き取るのが好
適である。
In order to obtain the full effect of the present invention, it is preferable to make the packed state of the particulate activated carbon as dense as possible before pressing the layer of particulate activated carbon.
For this reason, generally a cylindrical filling container with entrances and exits at both ends is set up almost vertically, one filter is loaded at the bottom of the container, and while the container is appropriately vibrated, particulate activated carbon is poured into the container along with water from above. Preferably, excess water is drained off through a filter at the bottom.

充填終了後上側フイルタを粒子状吸着剤層を押
圧しつつ装填し、必要によりポートキヤツプ等を
とりつけ、好ましくはその後清浄水を潅流し、充
填作業中に発生した吸着剤微粉末を洗浄する。洗
浄後フイルタの押圧力が低下している様なら、フ
イルタ位置を下げるか粒子状吸着剤を追加するか
して、押圧力を回復させる。押圧力は吸着剤粒子
を破壊しない範囲で大きいのが好ましく試行錯誤
により決定する。場合によつては、途中で熱処理
することにより粒子状吸着剤の充填密度を上げる
のが好ましい。さらに洗浄を続け、体液浄化器を
通過して来る洗浄水中に吸着剤微粉末がなくなれ
ば容器内の水を生理的食塩水と置換し、滅菌工程
に供する。
After filling is completed, the upper filter is loaded while pressing the particulate adsorbent layer, a port cap etc. is attached if necessary, and then clean water is preferably irrigated to wash away adsorbent fine powder generated during the filling operation. If the filter pressure has decreased after cleaning, lower the filter position or add particulate adsorbent to restore the filter pressure. The pressing force is preferably as large as possible without destroying the adsorbent particles, and is determined by trial and error. In some cases, it is preferable to increase the packing density of the particulate adsorbent by performing heat treatment during the process. The washing is continued further, and when there is no adsorbent fine powder in the washing water passing through the body fluid purifier, the water in the container is replaced with physiological saline, and the container is subjected to a sterilization process.

本発明では滅菌方法は、ガンマー線照射により
行う。熱を利用しない滅菌法としては、他に薬剤
による滅菌があるが、吸着剤による吸着の問題が
あるので利用できない。ガンマー線照射によつて
も若干の温度上昇が見られるので、なるべく強度
の低いガンマー線で時間をかけて照射するのが好
ましい。照射総線量は、体液浄化器内の菌数や採
用する安全係数により決定される。
In the present invention, the sterilization method is performed by gamma irradiation. Another sterilization method that does not use heat is sterilization using chemicals, but this cannot be used because of the problem of adsorption by adsorbents. Since a slight temperature increase is observed even with gamma ray irradiation, it is preferable to irradiate with gamma rays of as low intensity as possible over a long period of time. The total irradiation dose is determined by the number of bacteria in the body fluid purifier and the safety factor adopted.

〔発明の効果〕〔Effect of the invention〕

本発明に係る体液浄化器の製造法によれば、吸
着剤層の両側に張設したフイルタ部材を外方から
それぞれ可調整に押圧して活性炭等の粒子状吸着
剤を層内で移動しないように加圧保持することに
より、粒子状吸着剤の滅菌時の熱膨張および輸送
時の振動による吸着剤微粉末の発生を僅少に保つ
ことができる。
According to the method for manufacturing a body fluid purifier according to the present invention, the filter members stretched on both sides of the adsorbent layer are pressurized from the outside in an adjustable manner to prevent particulate adsorbent such as activated carbon from moving within the layer. By holding the particulate adsorbent under pressure, generation of fine adsorbent powder due to thermal expansion during sterilization of the particulate adsorbent and vibration during transportation can be kept to a minimum.

また、本発明の体液浄化器の製造法によれば、
前述した粒子状吸着剤層に対するフイルタ部材の
押圧装着を行つた後、前記吸着剤層に清浄水を潅
流し、充填作業中に発生した吸着剤微粉末を洗浄
し、この洗浄を完了した後容器内の水を生理的食
塩水と置換してガンマー線照射による滅菌を行う
ものであるから、本発明の製造法で得られた体液
浄化器はその使用直前に吸着剤微粉末を洗浄する
必要がなく、直ちに使用することができ、取扱い
が簡便となる。
Furthermore, according to the method for manufacturing a body fluid purifier of the present invention,
After the filter member is press-fitted onto the particulate adsorbent layer as described above, clean water is irrigated into the adsorbent layer to wash away adsorbent fine powder generated during the filling operation, and after this washing is completed, the container is removed. Since the water inside the body is replaced with physiological saline and sterilized by gamma ray irradiation, the body fluid purifier obtained by the production method of the present invention needs to be cleaned of the adsorbent fine powder immediately before use. It can be used immediately and is easy to handle.

本発明の用途として血液を主体に述べて来た
が、そのほか血液から分離された血漿など、人体
からとり出した体液から不要物を除去し、浄化さ
れた体液を人体に戻す場合に有効に利用できる。
また吸着剤として活性炭もしくは高分子被覆活性
炭について述べてきたが本発明はこれらに限定さ
れず、微粉末を発生し易い全ての吸着剤に有用で
ある。
Although the present invention has mainly been described as an application for blood, it can also be effectively used to remove unnecessary substances from body fluids taken out from the human body, such as plasma separated from blood, and to return the purified body fluids to the human body. can.
Furthermore, although activated carbon or polymer-coated activated carbon has been described as an adsorbent, the present invention is not limited thereto, and is useful for all adsorbents that tend to generate fine powder.

〔実施例〕〔Example〕

以下添付図面を参照しながら実施例により、本
発明による体液浄化器の製造法を説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS A method of manufacturing a body fluid purifier according to the present invention will be explained below by way of examples with reference to the accompanying drawings.

第1図および第2図において、筒体10は容器
本体であり、この中に粒子状吸着剤12を充填す
る。筒体10の端部にポート部材14を、弾性パ
ツキング16(たとえばゴムパツキング)を介し
て筒体内面に密接しつつ摺動自在に嵌入させる。
このパツキング16は、断面が円形のOリング、
断面がU字形のUリング、そのほか断面が台形の
もの等各種のものが使用できる。キヤツプ18
は、筒体10の外側からねじ込み式に装着され
て、ポート部材14を押圧しつつ自在の位置に固
定することができる。吸着剤の粒径より小さいメ
ツシユ寸法のスクリーンフイルタ20をポート部
材の内側に配置し、このフイルタはポート部材1
4を介するキヤツプ部からの押圧力を受けて粒子
状吸着剤12の層全体を押圧する。ポート部材1
4とフイルタ20との間にフイルタ補強用多孔板
22を設けて、スクリーンフイルタによる押圧力
の弱化を防ぐ。第2図に示した容器において、ポ
ート部材の固定可能な範囲を広くするため、ポー
ト部材の厚さLとキヤツプ内のねじ切り範囲lを
できるだけ、大きくしてある。
In FIGS. 1 and 2, a cylinder 10 is a container body, into which a particulate adsorbent 12 is filled. A port member 14 is slidably fitted into the end of the cylindrical body 10 through an elastic packing 16 (eg, rubber packing) while closely contacting the inner surface of the cylindrical body.
This packing 16 is an O-ring with a circular cross section,
Various types of rings such as U-rings with a U-shaped cross section and trapezoidal cross-sections can be used. cap 18
is screwed in from the outside of the cylindrical body 10, and can be fixed in any position while pressing the port member 14. A screen filter 20 having a mesh size smaller than the particle size of the adsorbent is placed inside the port member, and this filter is attached to the port member 1.
The entire layer of particulate adsorbent 12 is pressed by receiving the pressing force from the cap part via 4. Port member 1
A filter reinforcing porous plate 22 is provided between the screen filter 4 and the filter 20 to prevent the pressing force from being weakened by the screen filter. In the container shown in FIG. 2, in order to widen the range in which the port member can be fixed, the thickness L of the port member and the thread cutting range l in the cap are made as large as possible.

吸着剤としては、石油ピツチより作られたビー
ス活性炭にエチルヒドロキシエチルセルローズを
活性炭1g当たり2mg被覆したものを使用した。
As the adsorbent, beads activated carbon made from petroleum pit was coated with 2 mg of ethyl hydroxyethyl cellulose per gram of activated carbon.

実験1では筒体に下側のスクリーンフイルタ、
多孔板、ポート部材、弾性パツキング、キヤツプ
を装填し、筒体上部から、上述の活性炭を水とと
もに注入した。少量注入しては、筒体を外部より
たたいた。水が筒体上部からあふれそうになる
と、下部のポートから水を抜いた。この時水面が
粒子状吸着剤層上面より低くなると、以後に気泡
を混入するので、水面が下り過ぎない様に注意し
た。約300mlの粒子状吸着剤が充填された時点で
上側のフイルタ、多孔板、ポート部材、弾性パツ
キング、キヤツプを装填し、キヤツプをきつく締
めた。
In experiment 1, a lower screen filter was placed on the cylinder.
The perforated plate, port member, elastic packing, and cap were loaded, and the above-mentioned activated carbon was injected together with water from the top of the cylinder. After injecting a small amount, the cylinder was struck from the outside. When the water was about to overflow from the top of the cylinder, the water was drained from the port at the bottom. At this time, care was taken to ensure that the water level did not fall too low because if the water level became lower than the upper surface of the particulate adsorbent layer, air bubbles would be mixed in later. When approximately 300 ml of particulate adsorbent was filled, the upper filter, perforated plate, port member, elastic packing, and cap were loaded and the cap was tightly tightened.

次に上部ポート部から水を200ml/minの流量
で5時間流し、ポートにポートキヤツプ(図示せ
ず)をはめてガンマー線を2.5メガラツド照射し
た。
Next, water was flowed through the upper port at a flow rate of 200 ml/min for 5 hours, a port cap (not shown) was fitted to the port, and gamma rays were irradiated at 2.5 megarads.

実験2ではガンマー線滅菌を121℃20分の熱滅
菌に代えた。実験3では充填後キヤツプの締め不
充分のまま200ml/minの水で3時間洗浄し、ガ
ンマー線を照射した。
In Experiment 2, gamma ray sterilization was replaced with heat sterilization at 121°C for 20 minutes. In Experiment 3, after filling, the cap was not tightly tightened and was washed with water at 200 ml/min for 3 hours, followed by irradiation with gamma rays.

この3種類の体液浄化器中の吸着剤微粉末の量
を第3図に示す方法で評価した。
The amount of adsorbent fine powder in these three types of body fluid purifiers was evaluated by the method shown in FIG.

リザーバ30からの水をポンプ32により吸引
し、フイルタ34を通して清浄水となし、次いで
体液浄化器36の上方から下向流として押し込
み、体液浄化器の下方から押出された吸着剤粉末
を含有する清浄水を濾過容器38中に固定された
ます目入りフイルタ40に導入して、吸着剤粉末
をフイルタ40上に捕集する。減圧系42を必要
に応じて使用する。フイルタ34およびフイルタ
40は共に約1μ以上の粉末を捕捉すうるものを
用いた。フイルタ40上に捕集された吸着剤粉末
を顕微鏡下で計数した。
Water from the reservoir 30 is sucked by the pump 32, passed through the filter 34 to become clean water, and then forced into the body fluid purifier 36 as a downward flow from above, and the clean water containing the adsorbent powder pushed out from the bottom of the body fluid purifier 36. Water is introduced into a mesh filter 40 fixed in a filter vessel 38 and the adsorbent powder is collected on the filter 40. A vacuum system 42 is used as necessary. The filter 34 and the filter 40 were both capable of trapping powder of about 1 μm or more. The adsorbent powder collected on the filter 40 was counted under a microscope.

水を流量200ml/minで5分間流すことにより
フイルタ40に捕集された炭粉数は実験1で27
個、実験2で853個実験3で2196個であつた。
In experiment 1, the number of coal particles collected by the filter 40 by flowing water at a flow rate of 200 ml/min for 5 minutes was 27.
The number was 853 in Experiment 2 and 2196 in Experiment 3.

実験2では熱膨張時、吸着粒子が若干移動し、
粒子同士の摩擦があつたものと推定される。実験
3では粒子状活性炭が押圧されていないため、社
外へ照射依頼する時、輸送中の振動により粒子同
志または粒子と容器との間に摩擦が激しくおこつ
て吸着剤微粉末が多数発生したものと推定され
る。
In Experiment 2, the adsorbed particles moved slightly during thermal expansion;
It is presumed that this was caused by friction between the particles. In Experiment 3, the particulate activated carbon was not pressed, so when the irradiation was requested outside the company, the vibration during transportation caused intense friction between the particles or between the particles and the container, resulting in a large amount of fine adsorbent powder. It is estimated to be.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は実施例で用いた体液浄化器の斜視図、
第2図は第1図に示す体液浄化器の縦断面図、第
3図は吸着剤の流出粉末量を測定するシステムの
系統図である。 10……筒体、12……吸着剤、14……ポー
ト部材、16……パツキング、18……キヤツ
プ、20……フイルタ、22……補強用多孔板、
24……ポート部内腔、30……リザーバ、32
……ポンプ、34……フイルタ、36……体液浄
化器、38……濾過容器、40……フイルタ、4
2……減圧計。
FIG. 1 is a perspective view of the body fluid purifier used in the example.
FIG. 2 is a longitudinal sectional view of the body fluid purifier shown in FIG. 1, and FIG. 3 is a system diagram of a system for measuring the amount of adsorbent powder flowing out. 10... Cylindrical body, 12... Adsorbent, 14... Port member, 16... Packing, 18... Cap, 20... Filter, 22... Porous plate for reinforcement,
24... Port lumen, 30... Reservoir, 32
... pump, 34 ... filter, 36 ... body fluid purifier, 38 ... filtration container, 40 ... filter, 4
2... Decompression gauge.

Claims (1)

【特許請求の範囲】 1 両端に入口部と出口部とを設けた筒体からな
る容器内に、活性炭等の粒子状吸着剤を充填して
吸着剤層を形成し、この吸着剤層の両側に吸着剤
の粒径より小さいメツシユ寸法のフイルタ部材を
張設して体液浄化器を構成し、 前記吸着剤層の両側に張設したフイルタ部材を
外方からそれぞれ可調整に押圧して粒子状吸着剤
を層内で移動しないように加圧保持し、次いで前
記粒子状吸着剤を洗浄して微粉末等を除去した後
ガンマー線照射による滅菌を行うことを特徴とす
る体液浄化器の製造法。 2 特許請求の範囲第1項記載の体液浄化器の製
造法において、両端を開口した筒体からなる容器
内に粒子状吸着剤を充填して吸着剤層を形成し、
この吸着剤層の両側にそれぞれ吸着剤の粒径より
小さいメツシユ寸法の入口側フイルタと出口側フ
イルタとを張設し、前記各フイルタの外方からそ
の周縁部に対し当接してこれを押圧するポート部
材をそれぞれ容器の両端内周面に密接させて挿入
配置し、これらポート部材を外方から可調整に押
圧保持すると共に前記フイルタを介して粒子状吸
着剤を加圧するキヤツプをそれぞれ容器の両端に
装着してなる体液浄化器の製造法。
[Claims] 1. A container consisting of a cylinder with an inlet and an outlet at both ends is filled with particulate adsorbent such as activated carbon to form an adsorbent layer, and both sides of the adsorbent layer are filled with a particulate adsorbent such as activated carbon. A body fluid purifier is constructed by extending a filter member with a mesh size smaller than the particle size of the adsorbent layer, and adjustingly presses the filter members provided on both sides of the adsorbent layer from the outside to remove particles. A method for manufacturing a body fluid purifier, characterized in that the adsorbent is held under pressure so that it does not move within the layer, and then the particulate adsorbent is washed to remove fine powder, etc., and then sterilized by gamma ray irradiation. . 2. In the method for manufacturing a body fluid purifier according to claim 1, a container consisting of a cylindrical body with both ends open is filled with particulate adsorbent to form an adsorbent layer,
An inlet-side filter and an outlet-side filter each having a mesh size smaller than the particle size of the adsorbent are installed on both sides of the adsorbent layer, and are pressed against the peripheral edge of each filter by coming into contact with it from the outside. Port members are inserted and arranged in close contact with the inner circumferential surfaces of both ends of the container, and caps that adjustably press and hold these port members from the outside and pressurize the particulate adsorbent via the filter are installed at both ends of the container. A method for manufacturing a body fluid purifier that is attached to a person.
JP57030358A 1982-02-26 1982-02-26 Production of body liquid washer Granted JPS58146354A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57030358A JPS58146354A (en) 1982-02-26 1982-02-26 Production of body liquid washer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57030358A JPS58146354A (en) 1982-02-26 1982-02-26 Production of body liquid washer

Publications (2)

Publication Number Publication Date
JPS58146354A JPS58146354A (en) 1983-08-31
JPS6350021B2 true JPS6350021B2 (en) 1988-10-06

Family

ID=12301631

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57030358A Granted JPS58146354A (en) 1982-02-26 1982-02-26 Production of body liquid washer

Country Status (1)

Country Link
JP (1) JPS58146354A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007069983A1 (en) 2005-12-13 2007-06-21 Exthera Ab Method for extracorporeal removal of a pathogenic microbe, an inflammatory cell or an inflammatory protein from blood
US8758286B2 (en) 2009-12-01 2014-06-24 Exthera Medical Corporation Method for removing cytokines from blood with surface immobilized polysaccharides
ES2647577T3 (en) 2012-06-13 2017-12-22 Exthera Medical Corporation Use of heparin and carbohydrates to treat cancer
CN110772677A (en) 2013-06-24 2020-02-11 艾克塞拉医疗公司 Blood filtration system comprising mannose coated substrate
WO2015069942A1 (en) 2013-11-08 2015-05-14 Exthera Medical Corporation Methods for diagnosing infectious diseases using adsorption media
JP2017513636A (en) 2014-04-24 2017-06-01 エクスセラ メディカル コーポレイション Method for removing bacteria from blood using high flow rate
JP7100454B2 (en) * 2014-09-22 2022-07-13 エクスセラ メディカル コーポレイション Wearable blood perfusion device
US11911551B2 (en) 2016-03-02 2024-02-27 Exthera Medical Corporation Method for treating drug intoxication
WO2017151797A1 (en) 2016-03-02 2017-09-08 Exthera Medical Corporation Method for treating drug intoxication

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5663358A (en) * 1979-10-29 1981-05-29 Terumo Corp Purifier for body fluid
JPS57103649A (en) * 1980-12-18 1982-06-28 Asahi Chemical Ind Sterilized gamma-globulin fixing column
JPS5854959A (en) * 1981-09-25 1983-04-01 旭化成株式会社 Production of immune adsorbing apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5663358A (en) * 1979-10-29 1981-05-29 Terumo Corp Purifier for body fluid
JPS57103649A (en) * 1980-12-18 1982-06-28 Asahi Chemical Ind Sterilized gamma-globulin fixing column
JPS5854959A (en) * 1981-09-25 1983-04-01 旭化成株式会社 Production of immune adsorbing apparatus

Also Published As

Publication number Publication date
JPS58146354A (en) 1983-08-31

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