JPS60132566A - Production of medical hollow yarn mambrane - Google Patents

Production of medical hollow yarn mambrane

Info

Publication number
JPS60132566A
JPS60132566A JP24289183A JP24289183A JPS60132566A JP S60132566 A JPS60132566 A JP S60132566A JP 24289183 A JP24289183 A JP 24289183A JP 24289183 A JP24289183 A JP 24289183A JP S60132566 A JPS60132566 A JP S60132566A
Authority
JP
Japan
Prior art keywords
hollow fiber
water
spinning
fiber membrane
manufacturing
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.)
Granted
Application number
JP24289183A
Other languages
Japanese (ja)
Other versions
JPH0443690B2 (en
Inventor
木村 孝司
力 川村
勝 金泉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyobo Co Ltd
Original Assignee
Toyobo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP24289183A priority Critical patent/JPS60132566A/en
Publication of JPS60132566A publication Critical patent/JPS60132566A/en
Publication of JPH0443690B2 publication Critical patent/JPH0443690B2/ja
Granted legal-status Critical Current

Links

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は医療用中空糸膜の製造方法に関する。[Detailed description of the invention] The present invention relates to a method for producing a medical hollow fiber membrane.

高分子重合体から成る多孔質中空糸膜は選択透過性能を
有し、その性質を生かして色々な用途に使われている。
Porous hollow fiber membranes made of high molecular weight polymers have selective permeation performance, and are used in a variety of applications by taking advantage of this property.

その中空糸膜の製造に際し、て原料組成、中空糸膜形成
の方法、後処理の方法等を使への進出は目ざましいもの
があり、特に人工透析用の中空糸膜はその適用を受ける
べき腎疾患者が多いことも相まって増産の一途をたどっ
ている。
In the production of hollow fiber membranes, there has been a remarkable advance in the use of raw material composition, hollow fiber membrane formation methods, post-treatment methods, etc., and in particular, hollow fiber membranes for artificial dialysis are being applied to the kidneys. Coupled with the large number of sick people, production continues to increase.

一方、医療分野を対象とする中空糸膜は製造からユーザ
ーに供されるまで、安全衛生面において十分な配慮がな
されなGjればならない。
On the other hand, hollow fiber membranes intended for the medical field must be given sufficient consideration in terms of health and safety from manufacture to delivery to users.

高分子化合物を、溶剤に溶解させて紡糸原液とし、この
紡糸原液を紡糸ノズルがら芯液と共に押し出し、凝固さ
せた後洗浄して溶剤を除去するような中空糸膜製造方法
においてその洗浄剤として特殊な薬剤を使ったり、不純
物を含有する水を使う場合があるが、これらではそれら
の薬剤や不純物が中空糸膜に残留し医療用中空糸膜とし
てははなはだ不適当である。また菌を含有する水を使う
ことも、中空糸膜に菌を(寸着させる結果になり好まし
くない。菌は通常いたるところに存在し、ちよっとした
油断で容易に中空糸膜製造工程に混入するし、菌の平均
間代時間はその種類によっても異なるが数十分から数時
間であり、このことは一度混入した菌は容易に増殖する
ことを意味する。
Specially used as a cleaning agent in hollow fiber membrane manufacturing methods in which a polymer compound is dissolved in a solvent to form a spinning stock solution, this spinning stock solution is extruded together with a core solution through a spinning nozzle, solidified, and then washed to remove the solvent. In some cases, chemicals or water containing impurities are used, but in these cases, these chemicals and impurities remain in the hollow fiber membrane, making it extremely unsuitable for use as a medical hollow fiber membrane. Furthermore, using water containing bacteria is also undesirable as it can cause bacteria to adhere to the hollow fiber membrane.Bacteria are usually present everywhere, and a slight lapse of care can easily interfere with the hollow fiber membrane manufacturing process. The average clonic time of bacteria varies depending on the type, but it ranges from several tens of minutes to several hours, which means that once contaminated, bacteria can easily multiply.

医療器機の製造にあたっては清浄な室いわゆるクリーン
ルームで行なわれるのが通常であるがそれでもなお楽観
はできない。
Although the manufacturing of medical devices is normally carried out in clean rooms, it is still difficult to be optimistic.

通常医療用中空糸はモジュールに作成され、ユーザーに
供されるまでの間に滅菌の一工程を経て安全性が高めら
れている。モジュール作成までにその中空糸が菌を含有
していたならば滅菌の工程で生菌をなくすることはでき
るものの、例えばパイロジエン(発熱性物質)等は含有
しているおそれがある。
Typically, medical hollow fibers are made into modules and undergo a sterilization process before being delivered to the user, increasing safety. If the hollow fibers contain bacteria before the module is created, viable bacteria can be eliminated in the sterilization process, but there is a risk that they may still contain, for example, pyrogienes (pyrogens).

本発明者端は閑のイ」着していない医療用中空糸膜を得
るための手段について鋭意検削の結果本発明を見い出す
に主っだ。
The inventor of the present invention discovered the present invention as a result of intensive research into methods for obtaining hollow fiber membranes for medical use, which are not currently available.

即ち、本発明は高分子化合物を溶剤に溶解させて紡糸原
液としこの紡糸原液を紡糸ノズルから芯液と共に押し出
しめ・固さセた後洗浄して紡糸原液の溶剤を除去する医
療用中空糸膜製造方法において、その洗浄水として無菌
水を使用することを特徴をおくものである。
That is, the present invention provides a medical hollow fiber membrane in which a polymer compound is dissolved in a solvent to form a spinning dope, and this spinning dope is extruded from a spinning nozzle together with a core liquid, and after the solidity is set, the solvent is removed from the spinning dope by washing. The manufacturing method is characterized in that sterile water is used as the washing water.

ここで本発明に用いる無菌水とは日本薬局方の無菌試験
法のメンブランフィルタ−法により試験し合格した水で
ある。
The sterile water used in the present invention is water that has been tested and passed by the membrane filter method of the sterility test method of the Japanese Pharmacopoeia.

本発明において使用する高分子化合物とは、格別限定を
設けるものでなくセルロースジアセテート、セルロース
トリアセテート等のセルロースエステル;銅アンモニア
法セルロース;ポリアクリロニトリル;ポリメチルメチ
クリレート;ポリエチレン;酢酸ビニル共重合体;ホリ
ビニルアルコール;ポリプロピレン等を挙番することが
できる。
The polymer compounds used in the present invention are not particularly limited, and include cellulose esters such as cellulose diacetate and cellulose triacetate; cuprammonium cellulose; polyacrylonitrile; polymethyl methacrylate; polyethylene; and vinyl acetate copolymer. ; holivinyl alcohol; polypropylene, etc. can be mentioned.

これらの高分子化合物は適当な溶剤に溶解し紡糸原液に
作製する。そしてこの紡糸原液を環状紡糸孔より紡出さ
せ必要に応じて空気中を走行せしめた後凝固させる。凝
固が完了した中空糸はこの後洗浄され、前記溶剤は除去
され医療用中空糸膜が製造される。本発明において重要
な点はかかる洗浄に際し洗浄水として無菌水を用いるこ
とにあかかる手段を採用することにより保有菌数の全く
ない中空糸膜が製造できた。かかる洗浄工程は一段の浴
、あるいは多段に分割された浴で行なわれるが好ましく
は洗浄の効率が高められる多段分割(数段〜士数段)の
方法である。この多段分割ではそれぞれの独立した浴に
新鮮な無菌水を流下させ中空糸膜を処理する。また万一
混入した生菌に対してその増殖を未然に防ぐために洗浄
工程に紫外線殺菌灯を設けることが好ましい。この様な
洗浄水は中空糸膜の走行する方向と逆方向に流下させる
These polymer compounds are dissolved in a suitable solvent to prepare a spinning stock solution. Then, this spinning dope is spun out from an annular spinning hole, passed through the air as required, and then solidified. The coagulated hollow fiber is then washed to remove the solvent and produce a medical hollow fiber membrane. The important point in the present invention is that by employing such a method of using sterile water as washing water during such washing, a hollow fiber membrane containing no bacteria could be produced. This washing step may be carried out in a single bath or in a bath divided into multiple stages, but preferably a multi-stage divided method (several stages to several stages) is preferred because it increases the cleaning efficiency. In this multistage division, fresh sterile water flows down into each independent bath to treat the hollow fiber membranes. In addition, it is preferable to provide an ultraviolet sterilizing lamp in the cleaning process in order to prevent the proliferation of viable bacteria that may have been contaminated. Such washing water is caused to flow down in the direction opposite to the direction in which the hollow fiber membrane runs.

この様に医療用中空糸膜の製造にあたり、洗浄水として
無菌水を用いることにより無菌状態の安全衛生面に充分
配慮のなされた中空糸膜がつくられこれは医療分野へ大
きく貢献できるものである。
In this way, when manufacturing hollow fiber membranes for medical use, by using sterile water as the washing water, hollow fiber membranes with sufficient consideration given to the safety and hygiene aspects of sterile conditions can be created, which can greatly contribute to the medical field. .

以下本発明の実施例を記載するが本発明はこれら実施例
によって何隻限定をうけるものでない。
Examples of the present invention will be described below, but the present invention is not limited to these examples.

実施例1〜3及び比較例1〜2 セルロースアセテート30重量部、ジメチルホルムアミ
ド49重量部、ポリエチレングリコール200を21重
量部を85℃で2時間攪拌して溶解し、紡糸原液を作製
した。この紡糸原液を85℃で2時間静置脱泡した。環
状オリフィスノズルを用いて紡糸を行なった。一方芯液
として流動ツクラフインを供給した。環状オリフィスを
出た中空状の原液を15cm空気中を走行させ、その後
凝固浴に導き凝固させその後水洗、洗浄した。この洗浄
には下記の3通りでその都度無菌水を調整し中空糸膜の
進行方向と逆方向に流下せしめ実施した。
Examples 1 to 3 and Comparative Examples 1 to 2 30 parts by weight of cellulose acetate, 49 parts by weight of dimethylformamide, and 21 parts by weight of polyethylene glycol 200 were stirred and dissolved at 85° C. for 2 hours to prepare a spinning stock solution. This spinning stock solution was left standing at 85° C. for 2 hours to defoam. Spinning was carried out using an annular orifice nozzle. On the other hand, fluidized rough-in was supplied as a core liquid. The hollow stock solution that came out of the annular orifice was allowed to travel 15 cm in the air, and then introduced into a coagulation bath where it was coagulated and then washed with water. This cleaning was carried out in the following three ways by adjusting sterile water each time and flowing it down in the direction opposite to the direction of travel of the hollow fiber membrane.

この後ボビン状に巻き上げた。After that, it was wound into a bobbin shape.

実施例1:洗浄工程のカナルを3セクシヨンに分割しそ
の各々のセクションの最後部に 無菌水を導入。
Example 1: The canal of the cleaning process was divided into three sections and sterile water was introduced at the end of each section.

実施例2;多段式カナルの3段各々のカナルを独立させ
各カナルの最後部に無菌水を導 入。
Example 2: The canals of each of the three stages of the multi-stage canal were made independent, and sterile water was introduced into the rearmost part of each canal.

実施例3;実施例2に同様であるが、更に各カナルに紫
外線殺菌灯照射を実施。
Example 3: Same as Example 2, but each canal was further irradiated with an ultraviolet germicidal lamp.

なお、比較として無菌水の代わりにイ詞ン交換水を使用
した例も検討した。
For comparison, we also considered an example in which sterile water was used instead of sterile water.

比較例1;実施例1に同様であるが勲菌水の代わりにイ
オン交換水を使用。
Comparative Example 1: Same as Example 1, but ion-exchanged water was used instead of bacterial water.

比較例2;実施例2に同様であるがカlF菌水の代わり
にイオン交換水を使用。
Comparative Example 2: Same as Example 2, but ion-exchanged water was used instead of CalF bacteria water.

上記実施例、比較例の経時的に行なった結果を第1表に
まとめた。
The results of the above Examples and Comparative Examples performed over time are summarized in Table 1.

(7i、下余白 第 1 表 〔註〕1)氷中菌において一般細菌は1 ml、当り 
大腸菌群は]00m7!当りの生菌数 2)中空糸膜の保有菌は一定量の中空糸膜から無菌水に
菌を抽出して測定 以上の結果より医療用中空糸膜の製造にあたり、洗浄水
として無菌水を用いれば保有状態の全くない医療用途に
適切な中空糸膜が作製されることがわかる。
(7i, bottom margin Table 1 [Notes] 1) For bacteria in ice, 1 ml of general bacteria
Coliform bacteria is] 00m7! Number of viable bacteria per hollow fiber membrane 2) The bacteria retained in a hollow fiber membrane is measured by extracting bacteria from a certain amount of the hollow fiber membrane into sterile water.Based on the above results, sterile water is used as washing water when manufacturing medical hollow fiber membranes. It can be seen that a hollow fiber membrane suitable for medical use without any retention state can be produced.

特許出願人 東洋紡績株式会社Patent applicant: Toyobo Co., Ltd.

Claims (1)

【特許請求の範囲】 1、 高分子化合物を溶剤に溶解させて紡糸原液とし、
この紡糸原液を紡糸ノズルから芯液と共に押出し凝固さ
せた後洗浄して紡糸原液の溶剤を除去する医療用中空糸
膜製造方法において、その洗浄水として無菌水を使用す
ることを特徴とする医療用中空糸膜の製造方法。 2、 洗浄の工程を多段に分割し、各々の段階に新鮮な
細菌水を導入して行なう特許請求の範囲第1項記載の製
造方法。 3、 洗浄の工程の各々の段階に紫外線殺菌灯を照射し
て行なう特許請求の範囲第1項及び第2項記載の製造方
法。
[Claims] 1. Dissolving a polymer compound in a solvent to obtain a spinning stock solution;
A method for producing a medical hollow fiber membrane in which the spinning dope is extruded together with a core liquid from a spinning nozzle, coagulated, and then washed to remove the solvent of the spinning dope, wherein sterile water is used as the washing water. Method for manufacturing hollow fiber membranes. 2. The manufacturing method according to claim 1, wherein the washing step is divided into multiple stages and fresh bacterial water is introduced into each stage. 3. The manufacturing method according to claims 1 and 2, wherein each step of the cleaning process is carried out by irradiating an ultraviolet germicidal lamp.
JP24289183A 1983-12-22 1983-12-22 Production of medical hollow yarn mambrane Granted JPS60132566A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24289183A JPS60132566A (en) 1983-12-22 1983-12-22 Production of medical hollow yarn mambrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24289183A JPS60132566A (en) 1983-12-22 1983-12-22 Production of medical hollow yarn mambrane

Publications (2)

Publication Number Publication Date
JPS60132566A true JPS60132566A (en) 1985-07-15
JPH0443690B2 JPH0443690B2 (en) 1992-07-17

Family

ID=17095759

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24289183A Granted JPS60132566A (en) 1983-12-22 1983-12-22 Production of medical hollow yarn mambrane

Country Status (1)

Country Link
JP (1) JPS60132566A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62117813A (en) * 1985-11-15 1987-05-29 Nikkiso Co Ltd Production of hollow fiber
JP2002361052A (en) * 2001-06-05 2002-12-17 Kurita Water Ind Ltd Ultrafilter membrane for manufacturing ultrapure water and its preliminary washing method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52148487A (en) * 1976-06-04 1977-12-09 Asahi Chem Ind Co Ltd Filter membrane of hollow fiber
JPS536627A (en) * 1976-07-08 1978-01-21 Nippon Zeon Co Ltd Hollow fibers

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52148487A (en) * 1976-06-04 1977-12-09 Asahi Chem Ind Co Ltd Filter membrane of hollow fiber
JPS536627A (en) * 1976-07-08 1978-01-21 Nippon Zeon Co Ltd Hollow fibers

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62117813A (en) * 1985-11-15 1987-05-29 Nikkiso Co Ltd Production of hollow fiber
JP2002361052A (en) * 2001-06-05 2002-12-17 Kurita Water Ind Ltd Ultrafilter membrane for manufacturing ultrapure water and its preliminary washing method

Also Published As

Publication number Publication date
JPH0443690B2 (en) 1992-07-17

Similar Documents

Publication Publication Date Title
US5258149A (en) Process of making a membrane for high efficiency removal of low density lipoprotein-cholesterol from whole blood
JP3117575B2 (en) Polysulfone-based hollow fiber membrane and method for producing the same
AU660425B2 (en) High efficiency removal of low density lipoprotein-cholesterol from whole blood
JP4059543B2 (en) Medical device for extracorporeal treatment of blood or plasma and method for manufacturing the device
CN101703893B (en) Hollow fiber ultrafiltration composite membrane, preparation method and application thereof
US5187010A (en) Membrane having high affinity for low density lipoprotein-cholesterol from whole blood
US5418061A (en) Microporous polysulfone supports suitable for removal of low density lipoprotein-cholesterol
EP0066408B1 (en) Porous membrane
US7087168B2 (en) Hollow fiber membrane for purifying blood
JP2000140589A (en) Porous polysulfone film
JPH06238139A (en) Polysulfone semipermeable membrane and its production
JP2000296318A (en) Polysulfone-base blood treatment module
US6632359B1 (en) Blood purifying apparatus
JPS60132566A (en) Production of medical hollow yarn mambrane
JP2832835B2 (en) Virus removal method
GB2086798A (en) Microporous cellulose membrane
JPH053335B2 (en)
JP2005137996A (en) Permselective separation membrane
JPH06200407A (en) Hollow yarn and its production
WO1995024262A1 (en) Hollow-fiber blood-purifying membrane and process for producing the same
JPH03196819A (en) Method for removing mycoplasma
JPH0366380A (en) Hollow fiber type plasma separating membrane
JPH03228671A (en) Porous regenerated cellulose membrane for removing mycoplasma and removal of mycoplasma
JP2009078121A (en) Blood purifier and its production method
JP2005007004A (en) Hollow fiber type body fluid treatment apparatus, hollow fiber bundle used therefor, and method for producing them