JPH02218374A - Sterilization processing for hollow fiber type blood processing device and the sterilized device - Google Patents
Sterilization processing for hollow fiber type blood processing device and the sterilized deviceInfo
- Publication number
- JPH02218374A JPH02218374A JP1039690A JP3969089A JPH02218374A JP H02218374 A JPH02218374 A JP H02218374A JP 1039690 A JP1039690 A JP 1039690A JP 3969089 A JP3969089 A JP 3969089A JP H02218374 A JPH02218374 A JP H02218374A
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- salt
- processing device
- blood processing
- fiber membrane
- 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
Links
- 239000012510 hollow fiber Substances 0.000 title claims abstract description 85
- 239000008280 blood Substances 0.000 title claims abstract description 53
- 210000004369 blood Anatomy 0.000 title claims abstract description 53
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 36
- 238000004659 sterilization and disinfection Methods 0.000 title claims abstract description 25
- 150000003839 salts Chemical class 0.000 claims abstract description 31
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 10
- 239000000463 material Substances 0.000 claims abstract description 7
- 229920002678 cellulose Polymers 0.000 claims abstract description 5
- 239000001913 cellulose Substances 0.000 claims abstract description 5
- 239000011780 sodium chloride Substances 0.000 claims abstract description 5
- 239000012266 salt solution Substances 0.000 claims abstract description 4
- 239000012528 membrane Substances 0.000 claims description 52
- 238000000034 method Methods 0.000 claims description 18
- 230000017531 blood circulation Effects 0.000 claims description 8
- 230000005855 radiation Effects 0.000 claims description 6
- 238000004382 potting Methods 0.000 claims description 3
- 238000000502 dialysis Methods 0.000 abstract description 6
- 230000037452 priming Effects 0.000 abstract description 5
- 230000002633 protecting effect Effects 0.000 abstract description 3
- 230000002542 deteriorative effect Effects 0.000 abstract description 2
- 230000002285 radioactive effect Effects 0.000 abstract 2
- 239000007788 liquid Substances 0.000 abstract 1
- 235000002639 sodium chloride Nutrition 0.000 description 21
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 13
- 239000000243 solution Substances 0.000 description 12
- 235000011187 glycerol Nutrition 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 239000007864 aqueous solution Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000002504 physiological saline solution Substances 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 230000006866 deterioration Effects 0.000 description 3
- 229920002239 polyacrylonitrile Polymers 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000000108 ultra-filtration Methods 0.000 description 3
- 229920002301 cellulose acetate Polymers 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- DDRJAANPRJIHGJ-UHFFFAOYSA-N creatinine Chemical compound CN1CC(=O)NC1=N DDRJAANPRJIHGJ-UHFFFAOYSA-N 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 2
- 239000004926 polymethyl methacrylate Substances 0.000 description 2
- 229920002689 polyvinyl acetate Polymers 0.000 description 2
- 239000011118 polyvinyl acetate Substances 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 102100040678 Programmed cell death protein 1 Human genes 0.000 description 1
- 101710089372 Programmed cell death protein 1 Proteins 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 229940109239 creatinine Drugs 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000003670 easy-to-clean Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000005251 gamma ray Effects 0.000 description 1
- 150000002314 glycerols Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 229920002050 silicone resin Polymers 0.000 description 1
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
- External Artificial Organs (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野」
この発明は、中空糸膜を利用して血液の浄化処理(透析
)を行なう中空糸膜型血液処理装置の滅菌処理を内部の
中空糸を劣化させることなく行うことのできる滅菌処理
方法、および使用に先立って行われるブライミングを容
易に行うことのできる滅菌処理済み中空糸膜型血液処理
装置に関するものである。Detailed Description of the Invention "Field of Industrial Application" This invention is a method for sterilizing a hollow fiber membrane type blood processing device that performs blood purification (dialysis) using a hollow fiber membrane. The present invention relates to a sterilization method that can be performed without deterioration, and a sterilized hollow fiber membrane type blood processing device that can be easily brimmed before use.
「従来の技術」
周知のように、血液の浄化処理を人工的に行なう医療装
置として、透析膜に中空糸膜を使用した構造の中空糸膜
型血液処理装置が知られて(Xる。``Prior Art'' As is well known, a hollow fiber membrane type blood processing device that uses a hollow fiber membrane as a dialysis membrane is known as a medical device that artificially performs blood purification processing (X).
すなわち、多数の中空糸膜により容器内に多数の血液流
通路と透析液流路とを形成し、上記中空糸膜を介して血
液と透析液とを接触させ、血液中の老廃物を透析液中に
排出させる構造の装置である。That is, a large number of blood flow paths and dialysate flow paths are formed in the container using a large number of hollow fiber membranes, and the blood and dialysate are brought into contact through the hollow fiber membranes, and waste products in the blood are transferred to the dialysate. This is a device designed to discharge water inside.
このような血液処理装置として、従来、第1図に示す構
造のものが知られている。As such a blood processing apparatus, one having the structure shown in FIG. 1 is conventionally known.
図中符号lは円筒状の筒体を示すもので、この筒体1の
両端部は拡径されて筒体頭部2a、 2bとなっている
。この筒体頭部2a、 2bの側部には透析液を上記筒
体1中に導入し、筒体1外に排出する流通管3a、 3
bが設けられている。Reference numeral 1 in the figure indicates a cylindrical body, and both ends of this cylindrical body 1 are enlarged in diameter to form cylinder heads 2a and 2b. At the sides of the cylinder heads 2a, 2b are flow pipes 3a, 3 for introducing the dialysate into the cylinder 1 and discharging it outside the cylinder 1.
b is provided.
前記構成の筒体1内には多数の中空糸(透析膜)4が集
束状態で収められている。これら中空糸4は、セルロー
ス膜、CA(セルロースアセテート)膜、PAN (、
ポリアクリロニトリル)膜、PMMA(ポリメタクリル
酸メチル)膜、PVA (ポリ酢酸ビニル)膜、などの
生体適合性がよく、透析性のある合成膜から構成され、
内径30−1000μ肩であり、内部に血液を流通させ
るものである。A large number of hollow fibers (dialysis membranes) 4 are housed in a bundled state in the cylinder 1 having the above structure. These hollow fibers 4 are cellulose membranes, CA (cellulose acetate) membranes, PAN (,
It is composed of biocompatible and dialyzable synthetic membranes such as polyacrylonitrile (polyacrylonitrile) membrane, PMMA (polymethyl methacrylate) membrane, and PVA (polyvinyl acetate) membrane.
It has an inner diameter of 30-1000μ and allows blood to flow inside.
前記収束状態の中空糸4・・・・・・は、筒体1内に収
納後にその両端部をポリウレタン樹脂、シ1ノコーン樹
脂などのボ・ソテイング材5.5により上38簡体l内
において固定されており、このポ・ノテイング材5.5
の外側端面には前記中空糸4・・・・・・力(開口して
いる。After the hollow fibers 4 in the converged state are housed in the cylinder 1, both ends of the hollow fibers 4 are fixed in the upper 38 simplified body 1 with a sautéing material 5.5 such as polyurethane resin or silicone resin. This po-noting material is 5.5
The hollow fibers 4 are open on the outer end surface thereof.
そして、この筒体1には、その両開口部6a、6bを覆
うようにして蓋体7.8が嵌着、固定さ4tている。こ
の蓋体7.8はキヤ・ノブ状に形成されており、この蓋
体7.8と前記筒体頭部2a、2blよ接着されており
、蓋体7.8〜筒体1間力く気密槽5告となっている。A lid 7.8 is fitted and fixed to the cylinder 1 so as to cover both openings 6a and 6b. This lid 7.8 is formed into a can-knob shape, and the lid 7.8 and the cylinder head 2a, 2bl are glued together, and the lid 7.8 and the cylinder 1 are tightly connected. There are 5 airtight tanks.
そして、上方の蓋体8には血液流通突管9aが設けられ
、下方の蓋体71こ(ま血液流通突管9bが設けられて
おり、上方の血液流通突管9aから蓋体8内に血液を流
入させ、さら(こ各中空糸4・・・・・・内に血液を流
入させ、下方の蓋体7の血液流通突管9bから血液を流
出させるよう(こなって(Xる。The upper lid body 8 is provided with a blood circulation tube 9a, and the lower lid body 71 is provided with a blood circulation tube 9b. The blood is allowed to flow in, and further into each hollow fiber 4, and the blood is caused to flow out from the blood circulation tube 9b of the lower lid 7.
上記構成において、透析液は各中空糸4・・・間を通り
、これら中空糸膜を介して血液中の老廃物が中空糸4外
の透析液中に排出され、これ(こよりて血液の浄化が行
われる。In the above configuration, the dialysate passes between the hollow fibers 4, and waste products in the blood are discharged into the dialysate outside the hollow fibers 4 through these hollow fiber membranes. will be held.
ところで、このような構成、作用を有する中空糸膜型血
液処理装置は、完成製品(内部に水、溶液などが充填さ
れていない乾燥状態の製品)とする前に滅菌処理を行わ
なければならない。滅菌はオートクレーブ滅菌や放射線
(γ線)滅菌により行っているが、単にそのまま滅菌す
ると、セルロース系膜などから構成されている中空糸が
温度上昇等により劣化してしまうので、従来、滅菌工程
の前に筒体内に膜保護剤としてグリセリン水溶液(5〜
40%濃度)を流通されることによりグリセリンを中空
糸膜に付着させていた。このように、従来の中空糸膜型
血液処理装置では、筒体内にグリセリン水溶液を流通さ
せて、グリセリンを中空糸膜に付着させることによって
、中空糸に劣化を引き起こすことなく滅菌を完了するこ
とができており、滅菌済みの製品にはグリセリンが付着
している。By the way, a hollow fiber membrane type blood processing device having such a configuration and function must be sterilized before being made into a finished product (a dry product with no water, solution, etc. filled inside). Sterilization is performed by autoclave sterilization or radiation (gamma ray) sterilization, but if the hollow fibers are simply sterilized as they are, the hollow fibers made of cellulose membranes will deteriorate due to temperature rise, etc. In addition, a glycerin aqueous solution (5~
40% concentration) to adhere to the hollow fiber membrane. In this way, in conventional hollow fiber membrane blood processing devices, sterilization can be completed without causing deterioration of the hollow fibers by circulating an aqueous glycerin solution inside the cylinder and attaching glycerin to the hollow fiber membranes. The sterilized product is coated with glycerin.
「発明が解決しようとする課題」
ところで、前記従来の中空糸膜型血液処理装置の滅菌処
理方法では、次のような問題点が発生しており、その解
決が望まれているのが現状である。"Problems to be Solved by the Invention" By the way, the following problems have occurred in the conventional sterilization method for hollow fiber membrane type blood processing devices, and it is currently desired to solve them. be.
すなわち、筒体内および中空糸表面にはグリセリンが付
着しており、このグリセリンのために、装置の使用前に
行わなければならないブライミングが大変行いにくり、
装置の準備処理に時間がかかってしまう、という問題点
である。In other words, glycerin is attached to the inside of the cylinder and the surface of the hollow fibers, and this glycerin makes briming, which must be performed before using the device, very difficult.
The problem is that it takes time to prepare the device.
これに対し、洗浄の容易なアルコールや水を中空糸表面
に付着させる方法も考えられる。しかし、水の場合は、
単に中空糸の表面が濡れている程度の量だけでは中空糸
保護効果がなく、ある程度、滅菌後にも筒体内に水が残
っていないと効果が発揮されないため、製品は乾式の装
置ではなくなってしまう、という問題点があり、実用的
ではない。On the other hand, a method of attaching alcohol or water, which is easy to clean, to the hollow fiber surface may also be considered. However, in the case of water,
If the surface of the hollow fiber is simply wet, it will not have a protective effect on the hollow fiber, and the product will not be effective unless some water remains inside the cylinder even after sterilization, so the product is no longer a dry device. , and is not practical.
また、アルコールを用いる方法では、滅菌に伴う加熱に
対して爆発性があり、危険であり、またアルコール上記
は有害である、という問題点があり、製造上に困難があ
る。Furthermore, the method using alcohol has the problem that it is explosive and dangerous when heated during sterilization, and alcohol is harmful, making it difficult to manufacture.
この発明は、かかる事情に鑑みてなされたもので、中空
糸膜を利用して血液の浄化処理(透析)を行なう中空糸
膜型血液処理装置の滅菌処理を内部の中空糸を劣化させ
ることなく行うことのできる滅菌処理方法、および使用
に先立って行われるブライミングを容易に行うことので
きる滅菌処理済み中空糸膜型血液処理装置を提供するこ
とを課題とするものである。This invention was made in view of the above circumstances, and it is possible to sterilize a hollow fiber membrane type blood processing device that performs blood purification (dialysis) using hollow fiber membranes without deteriorating the internal hollow fibers. It is an object of the present invention to provide a sterilization method that can be used and a sterilized hollow fiber membrane type blood processing device that can be easily brimmed before use.
「課題を解決するための手段」
本発明者らは、上記従来の課題を解決するために鋭意研
究を重ねたところ、下記のような知見を得るに至った。"Means for Solving the Problems" The present inventors have conducted extensive research to solve the above-mentioned conventional problems, and have come to the following findings.
すなわち、滅菌に対する中空糸の保護材料として塩を用
いれば、はとんど水のない状態で中空糸に付着させても
、充分に中空糸保護効果が発揮され、しかも、塩は容易
に洗浄することができるので、ブライミングがたいへん
容易であることが判明した。なお、使用する塩の付着量
は、中空糸重量の2〜40%が好ましい。というのは、
2%未満であると、充分な中空糸保護効果が得られなく
なり、逆に40%を越えると、中空糸内に多量の塩結晶
が生じるためにブライミングが行いにくくなるからであ
る。また、使用する塩としては、生体適合性から考慮し
て食塩が最も好ましい。In other words, if salt is used as a protective material for hollow fibers against sterilization, the salt will have a sufficient effect of protecting the hollow fibers even if it is attached to the hollow fibers in the absence of water, and moreover, salt can be easily washed away. It has been found that briming is very easy. The amount of salt used is preferably 2 to 40% of the weight of the hollow fibers. I mean,
If it is less than 2%, a sufficient hollow fiber protection effect cannot be obtained, and if it exceeds 40%, a large amount of salt crystals will be generated within the hollow fibers, making it difficult to perform briming. Moreover, as the salt to be used, common salt is most preferable in view of biocompatibility.
本発明はかかる知見に基づいてなされたものである。The present invention has been made based on this knowledge.
すなわち、本発明方法は、筒体内に塩溶液を流通、通過
させて、筒体内の中空糸膜の全表面に塩を付着させる前
処理工程と、前記中空糸膜型血液処理装置をオートクレ
ーブ滅菌装置または放射線滅菌装置により滅菌を行う滅
菌工程とからなる中空糸膜型血液処理装置の滅菌処理方
法であり、また、本発明装置は、各中空糸の全外表面に
塩が付着していることを特徴とする滅菌処理済み中空糸
膜型血液処理装置である。That is, the method of the present invention includes a pretreatment step in which a salt solution is circulated and passed through the cylinder to adhere salt to the entire surface of the hollow fiber membrane in the cylinder, and the hollow fiber membrane type blood processing apparatus is sterilized in an autoclave. or a sterilization step of sterilizing with a radiation sterilizer, the method of the present invention is a method for sterilizing a hollow fiber membrane type blood processing device, and the device of the present invention is capable of sterilizing the entire outer surface of each hollow fiber. This is a sterilized hollow fiber membrane type blood processing device.
「作用」
前記構成の中空糸型血液処理装置によれば、中空糸の全
面に付着している塩は、熱や放射線による負荷を和らげ
、滅菌工程によって中空糸膜を劣化させることがない。"Function" According to the hollow fiber blood processing device having the above configuration, the salt adhering to the entire surface of the hollow fibers relieves the load caused by heat and radiation, and the hollow fiber membranes do not deteriorate during the sterilization process.
また、このような作用を起こす塩の付着形態は、特に水
分を必要としないので、容易に乾式の装置を提供するこ
とができる。Furthermore, since the form of salt deposition that causes such an effect does not particularly require moisture, a dry type device can be easily provided.
さらに、使用前に行う溶液による洗浄、充填も溶解性の
高い塩であるため、たいへん効率よく行うことができる
。ブライミング用溶液は、通常生理的食塩水が用いられ
るので、付着用の塩として食塩を用いた場合、さらにブ
ライミングが容易かつ安全性の高いものになる。Furthermore, cleaning and filling with a solution before use can be carried out very efficiently since the salt is highly soluble. Since physiological saline is usually used as the briming solution, briming becomes easier and safer when saline is used as the adhesion salt.
以下、この発明の実施例を示す。Examples of this invention will be shown below.
「実施例」
第1図に示す構造の装置において、筒体1内に約1%濃
度の食塩水■と、約25%濃度の食塩水■とをそれぞれ
流通することにより食塩の付着量が中空糸重量のそれぞ
れ2%(■)と40%(■)の状態にした。つづいて、
これら装置をオートクレーブ内に入れ、下記のような条
件にて滅菌を行った。"Example" In the device having the structure shown in Fig. 1, the amount of salt deposited is reduced by flowing saline solution ■ with a concentration of about 1% and saline solution ■ with a concentration of about 25% into the cylinder 1. The yarn weight was 2% (■) and 40% (■), respectively. Continuing,
These devices were placed in an autoclave and sterilized under the following conditions.
・蒸気温度・・・121 ’C
・時間・・・・・・・20分
これに対し、比較のために、従来通り約20%濃度のグ
リセリン水溶液を付着させた装置■を用意し、これも同
様に同じ条件下でオートクレーブにかけた。・Steam temperature: 121'C ・Time: 20 minutes On the other hand, for comparison, we prepared a device ■ to which a glycerin aqueous solution of about 20% concentration was attached as before, and this also It was also autoclaved under the same conditions.
このようにして、それぞれ滅菌処理を行った装置(有効
膜面積1.0m ’)■、■、■に対してクリアランス
と限外濾過率を測定した。クリアランス測定には、それ
ぞれ血液のかわりに尿素のイオン交換水溶液とクレアチ
ニンのイオン交換水溶液をそれぞれ100m12/ll
1in、 200m12 /sin、 300tQ/w
inと流量を変えて中空糸内を流すとともに、筒体内に
透析液のかわりに無成分イオン交換水を500m&/a
+inで流して、装置■、■、■のそれぞれにおいて装
置の中空糸の劣化度合いを調べた。In this way, the clearance and ultrafiltration rate were measured for each of the sterilized devices (effective membrane area: 1.0 m') (2), (2), and (2). For clearance measurement, use 100ml/ll of urea ion-exchanged aqueous solution and creatinine ion-exchanged aqueous solution instead of blood.
1in, 200m12/sin, 300tQ/w
In addition to changing the flow rate to flow inside the hollow fiber, 500 m&/a of non-component ion-exchanged water was poured into the cylinder instead of dialysate.
+in, and the degree of deterioration of the hollow fibers of the devices was examined in each of the devices ①, ②, and ②.
前記クリアランス(m12/m1n)は、次の式によっ
て求められるものである。The clearance (m12/m1n) is determined by the following formula.
Ct、= ((Cat cBo)/Ca1t X
QaQ a1=血液側溶液の入口側流量(m(/wi
n)、である。Ct, = ((Cat cBo)/Ca1t
QaQ a1 = Blood side solution inlet side flow rate (m(/wi
n).
一方、限外濾過率(U F R; mN/mmHg−h
r)の測定は、血液側および透析液側にイオン交換水液
を循環させ、血液側溶液の10分間の減少量から濾過量
(U F ;++ff/br)を求め、これをT M
P (mmHg)で割ったものである。TMPは以下の
式で求める。On the other hand, the ultrafiltration rate (UFR; mN/mmHg-h
To measure r), an ion-exchanged aqueous solution is circulated between the blood side and the dialysate side, and the filtration amount (U F ; ++ff/br) is determined from the amount of decrease in the blood side solution over 10 minutes.
It is divided by P (mmHg). TMP is calculated using the following formula.
TMP= ((Pao+Pat) (PDO+PD
1)) /2ここで、PBi=血液側の入口側圧力、
P Bo”血液側の出口側圧力、
P Dl”透析液側の入口側圧力、
Poo=透析液側の出口側圧力、
である。TMP= ((Pao+Pat) (PDO+PD
1)) /2 Here, PBi = inlet pressure on the blood side,
P Bo'' pressure on the outlet side of the blood side, P Dl'' pressure on the inlet side of the dialysate side, Poo = pressure on the outlet side of the dialysate side.
上式において、
C□=血液側溶液の入口側濃度、
CBo=血液側溶液の出口側濃度、
Co。=透析液側溶液の出口側濃度、
なお、この場合の血液側溶液の入口側流量は200/s
inで、同出口側流量は500m12として行われる。In the above equation, C□=inlet side concentration of blood side solution, CBo=outlet side concentration of blood side solution, Co. = outlet side concentration of dialysate side solution, In this case, the inlet side flow rate of blood side solution is 200/s
in, and the flow rate on the outlet side is 500 m12.
測定の結果を表1に示した。これらの表から明らかなよ
うに、本発明の装置■、■では、クリアランス(m12
/+n1n)も限外濾過率(fflQ/ffi11g−
hr)も共に従来の装置■と同等であり、滅菌処理によ
って、その中空糸膜に劣化が生じていないことが確認さ
れた。しかも、従来の装置と違って使用前に行うプライ
ミングは至極簡単に行うことができた。The measurement results are shown in Table 1. As is clear from these tables, the clearance (m12
/+n1n) and ultrafiltration rate (fflQ/ffi11g-
hr) were also the same as those of the conventional device (2), and it was confirmed that the hollow fiber membranes were not deteriorated by the sterilization treatment. Moreover, unlike conventional devices, priming before use can be performed extremely easily.
本発明装置■、■での生理的食塩水を用いて行ったプラ
イミングの完了までには、生理的食塩水が流量的8(L
J/minで5分を要したのに対し、従来装置■では生
理的食塩水が流量約80mff/m1nt’15分も必
要であった。By the time the priming using the physiological saline in the apparatuses (■) and (■) of the present invention is completed, the physiological saline has a flow rate of 8 (L).
J/min required 5 minutes, whereas in the conventional device (2), a flow rate of approximately 80 mff/ml of physiological saline was required for 15 minutes.
(以下、余白)
「発明の効果」
以上説明したように、本発明は、筒体内に塩溶液を流通
、通過させて、筒体内の中空糸膜の全表面に塩を付着さ
せる前処理工程と、前記中空糸膜型血液処理装置をオー
トクレーブ滅菌装置または放射線滅菌装置により滅菌を
行う滅菌工程とからなる中空糸膜型血液処理装置の滅菌
処理方法であり、
また、各中空糸の全外表面に塩が付着していることを特
徴とする滅菌処理済み中空糸膜型血液処理装置である。(Hereinafter, blank space) "Effects of the Invention" As explained above, the present invention includes a pretreatment step in which a salt solution is distributed and passed through the cylinder to adhere salt to the entire surface of the hollow fiber membrane inside the cylinder. , a method for sterilizing a hollow fiber membrane type blood processing device, which comprises a sterilization step of sterilizing the hollow fiber membrane type blood processing device using an autoclave sterilizer or a radiation sterilizer; This is a sterilized hollow fiber membrane type blood processing device characterized by the fact that salt is attached.
したがって、本発明によれば、中空糸の全表面に付着し
ている塩は、熱や放射線による負荷を和らげ、滅菌工程
によって中空糸を劣化させることがない。また、このよ
うな作用を起こす塩の付着形態は、特に水分を必要とし
ないので、容易に乾式の装置を提供することができる。Therefore, according to the present invention, the salt attached to the entire surface of the hollow fiber reduces the load caused by heat and radiation, and the hollow fiber does not deteriorate during the sterilization process. Furthermore, since the form of salt deposition that causes such an effect does not particularly require moisture, a dry type device can be easily provided.
さらに、使用前に行う溶液による洗浄、充填も溶解性の
高い塩であるため、たいへん効率よく行うことができる
。Furthermore, cleaning and filling with a solution before use can be carried out very efficiently since the salt is highly soluble.
プライミング用溶液は、通常生理的食塩水が用いられる
ので、付着用の塩として食塩を用いた場合、さらにブラ
イミングが容易かつ安全性の高いものになる。Physiological saline is usually used as the priming solution, so when salt is used as the adhesion salt, priming becomes easier and safer.
第1図は中空糸膜型血液処理装置の側断面図である。
■・・・・・・筒体、
2・・・・・・筒体頭部、
3a・・・・・・血液流入口、
3b・・・・・・血液流出口、
4・・・・・・中空糸(透析膜)、
5・・・・・・ポツティング材、
6a、 6b・・・・・筒体の開口部、7.8・・・・
・・蓋体、
9a・・・・・・血液流通突管、
9b・・・・・・血液流通突管。FIG. 1 is a side sectional view of a hollow fiber membrane type blood processing device. ■...Cylinder body, 2...Cylinder head, 3a...Blood inlet, 3b...Blood outlet, 4......・Hollow fiber (dialysis membrane), 5... Potting material, 6a, 6b... Opening of cylinder, 7.8...
...Lid body, 9a...Blood circulation tube, 9b...Blood circulation tube.
Claims (8)
内に外観柱状、に収束された多数の中空糸が収納される
とともに、その両端部がポッティング材により固定され
、血液の流通突管を有するキャップ状の蓋体が前記筒体
の両端部に一体に連結されてなる中空糸膜型血液処理装
置の滅菌処理方法であって、 前記筒体内に塩溶液を流通、通過させて、筒体内の中空
糸膜の全表面に塩を付着させる前処理工程と、 前記中空糸膜型血液処理装置をオートクレーブ滅菌装置
または放射線滅菌装置により滅菌を行う滅菌工程とから
なる中空糸膜型血液処理装置の滅菌処理方法。(1) A large number of hollow fibers converged into a columnar appearance are housed in a cylinder with dialysate flow tubes protruding from both ends, and both ends are fixed with potting material to prevent blood flow. A method for sterilizing a hollow fiber membrane type blood processing device in which a cap-like lid body having a flow tube is integrally connected to both ends of the cylinder body, the method comprising: circulating and passing a salt solution through the cylinder body; A hollow fiber membrane type blood processing device comprising a pretreatment step of attaching salt to the entire surface of the hollow fiber membrane in the cylinder, and a sterilization step of sterilizing the hollow fiber membrane type blood processing device using an autoclave sterilizer or a radiation sterilizer. Sterilization method for blood processing equipment.
とを特徴とする請求項1に記載の中空糸膜型血液処理装
置の滅菌処理方法。(2) The method for sterilizing a hollow fiber membrane type blood processing device according to claim 1, wherein the hollow fiber membrane is composed of a cellulose membrane.
求項1または2に記載の中空糸膜型血液処理装置の滅菌
処理方法。(3) The method for sterilizing a hollow fiber membrane type blood processing device according to claim 1 or 2, wherein the amount of salt attached is 2% to 40% of the weight of the hollow fibers.
ずれかに記載の中空糸膜型血液処理装置の滅菌処理方法
。(4) The method for sterilizing a hollow fiber membrane type blood processing device according to any one of claims 1 to 3, wherein the salt is sodium chloride.
内に外観柱状に収束された多数の中空糸が収納されると
ともに、その両端部がポッティング材により固定され、
血液の流通突管を有するキャップ状の蓋体が前記筒体の
両端部に一体に連結されてなり、 前記各中空糸の全外表面に塩が付着していることを特徴
とする滅菌処理済み中空糸膜型血液処理装置。(5) A large number of hollow fibers converged into a columnar appearance are housed in a cylinder with dialysate flow pipes protruding from both ends, and both ends are fixed with a potting material;
A cap-like lid body having a blood circulation protrusion is integrally connected to both ends of the cylindrical body, and the sterilized product is characterized in that salt is attached to the entire outer surface of each of the hollow fibers. Hollow fiber membrane type blood processing device.
を特徴とする請求項5に記載の滅菌処理済み中空糸膜型
血液処理装置。(6) The sterilized hollow fiber membrane type blood processing device according to claim 5, wherein the hollow fibers are made of a cellulose membrane.
求項5または6に記載の滅菌処理済み中空糸膜型血液処
理装置。(7) The sterilized hollow fiber membrane type blood processing device according to claim 5 or 6, wherein the amount of salt attached is 2% to 40% of the weight of the hollow fibers.
ずれかに記載の滅菌処理済み中空糸膜型血液処理装置。(8) The sterilized hollow fiber membrane type blood processing device according to any one of claims 5 to 7, wherein the salt is sodium chloride.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1039690A JPH02218374A (en) | 1989-02-20 | 1989-02-20 | Sterilization processing for hollow fiber type blood processing device and the sterilized device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1039690A JPH02218374A (en) | 1989-02-20 | 1989-02-20 | Sterilization processing for hollow fiber type blood processing device and the sterilized device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02218374A true JPH02218374A (en) | 1990-08-31 |
Family
ID=12560046
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1039690A Pending JPH02218374A (en) | 1989-02-20 | 1989-02-20 | Sterilization processing for hollow fiber type blood processing device and the sterilized device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02218374A (en) |
-
1989
- 1989-02-20 JP JP1039690A patent/JPH02218374A/en active Pending
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