JPS6341616B2 - - Google Patents
Info
- Publication number
- JPS6341616B2 JPS6341616B2 JP54139465A JP13946579A JPS6341616B2 JP S6341616 B2 JPS6341616 B2 JP S6341616B2 JP 54139465 A JP54139465 A JP 54139465A JP 13946579 A JP13946579 A JP 13946579A JP S6341616 B2 JPS6341616 B2 JP S6341616B2
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- cleaning
- fine particles
- cleaning liquid
- petroleum pitch
- 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
Links
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61M—DEVICES FOR INTRODUCING MEDIA INTO, OR ONTO, THE BODY; DEVICES FOR TRANSDUCING BODY MEDIA OR FOR TAKING MEDIA FROM THE BODY; DEVICES FOR PRODUCING OR ENDING SLEEP OR STUPOR
- A61M1/00—Suction or pumping devices for medical purposes; Devices for carrying-off, for treatment of, or for carrying-over, body-liquids; Drainage systems
- A61M1/36—Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits
- A61M1/3679—Other treatment of blood in a by-pass of the natural circulatory system, e.g. temperature adaptation, irradiation ; Extra-corporeal blood circuits by absorption
Landscapes
- Health & Medical Sciences (AREA)
- Heart & Thoracic Surgery (AREA)
- Vascular Medicine (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Anesthesiology (AREA)
- Biomedical Technology (AREA)
- Hematology (AREA)
- Cardiology (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Public Health (AREA)
- Veterinary Medicine (AREA)
- External Artificial Organs (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Carbon And Carbon Compounds (AREA)
Description
本発明は、人工肝、人工腎補助用などにコーテ
イングしないでそのまま用いる体液浄化用活性炭
の洗浄方法に関する。
従来、人工肝、人工腎補助用のDHPカラムに
使用される活性炭としては、ヤシガラ活性炭や石
油ピツチ活性炭があるが、ほとんどの場合これを
そのまま用いず活性炭に表面にコロジオン、ハイ
ドロゲル、セルロース等の高分子膜をコーテイン
グして使用している。コーテイングする理由は、
活性炭から微粒子(炭塵)が遊出するのを防止す
るとともに、微粒子に起因した血球の付着や血栓
の生成を防止できるようにして、活性炭に生体適
合性を与える為である。
しかし、コーテイングした活性炭は、表面が高
分子膜で覆われることから吸着能が低くなり、こ
の結果活性炭の使用量が多く装置が大型化し、こ
の結果プライミング量が多くなり、体外循環をす
る際に患者への負担が重くなり安全性で問題があ
る。しかもコーテイングした活性炭には、コーテ
イングする際使用する有機溶剤が多少残留し、又
オートクレーブ滅菌時、長期保存時にコーテイン
グ剤が溶出してくる可能性があり、これらが生体
に悪影響をおよぼすおそれがある。
これらのものとは別に、コーテイングしないヤ
シガラ活性炭をテープに粘着させて、微粒子の遊
出を防止するものがある。このものはコーテイン
グしないので吸着能は高いが装置が複雑で、コス
トが高くなり、しかも粘着剤を使用しているため
血液と接触する際、粘着剤から不純物が溶出する
おそれがある。
このように従来の血液浄化用活性炭において
は、いずれも吸着能あるいは生体適合性に問題が
ある。このため本発明者はこれらの問題を解決す
べく研究を行ない、その結果次のことを見出し
た。
すなわち、活性炭のうちヤシガラ活性炭は、そ
の表面の凹凸が激しく微粒子の量も極めて多い
が、これに比べて石油ピツチ活性炭は、表面が円
滑で、微粒子の量もさほどではなく、この活性炭
を十分洗浄して微粒子を剥離除去した場合、これ
をコーテイングせずにそのまま使用しても生体適
合性に問題がないことが判明した。
本発明は、このような知見にもとづいてなされ
たもので、石油ピツチ活性炭をそのままコーテイ
ングせずに使用する場合に、これを効率よくしか
も洗浄液を有効に利用して十分洗浄をおこなうこ
とができる体液浄化用活性炭の洗浄方法を提供す
るものである。
すなわち本発明は、石油ピツチ活性炭を超音波
洗浄機で洗浄して該石油ピツチ活性炭に付着した
微粒子を剥離除去する際に、上記洗浄機で該石油
ピツチ活性炭から除去した微粒子を含む洗浄液を
第1の濾過装置により微粒子を所定の大きさまで
濾過する工程と、第2の濾過装置でさらに該微粒
子を、より小さな大きさのものまで濾過する工程
と、第1及び第2の濾過工程で清浄化された洗浄
液を上記洗浄機に戻して循環使用する工程とから
なることを特徴とする体液浄化用活性炭の洗浄方
法である。
また本発明は、洗浄液及び洗浄される石油ピツ
チ活性炭を収納でき、さらに超音波発信手段を有
する超音波洗浄機と、該洗浄機の内部に連通し洗
浄液を循環させる洗浄液循環回路と、該回路中に
取付けられた洗浄液循環用ポンプと、上記回路内
と連通して洗浄液に含まれる微粒子を所定の大き
さまで濾過する第1の濾過装置と、更に該微粒子
を、より小さな大きさまで濾過する第2の濾過装
置とからなることを特徴とする体液浄化用活性炭
洗浄装置である。
以下、本発明の方法及び装置を図示する実施例
を参照して説明する。
第1図はこの方法に用いる洗浄装置を示した説
明図で、この洗浄装置は超音波洗浄機1、循環用
ポンプ2、第1及び第2の過装置3,4を設置
し、これらの間に洗浄液循環路5を形成してい
る。上記超音波洗浄機1は、超音波振動子6を備
えた浴槽7内に上記洗浄液循環路5のメツシユ付
液入口部8及び液出口部9を配置し、さらにモー
タ10で駆動される撹拌用プロペラ11を設けて
いる。この浴層7内には生理食塩水、蒸留水、デ
キストランなどの洗浄液12が満され、ここに石
油ピツチ活性炭13を入れる。この活性炭13と
しては、純度及び硬度が高く、遊出する微粒子の
少ないものが好ましい。又第1の過装置3は
5μのカートリツジフイルターを備え、又第2の
過装置4は1μのカートリツジフイルターを備
えている。
この洗浄装置において、超音波振動子6を作動
して石油ピツチ活性炭13に付着している微粒子
及び不純物を剥離除去して洗浄し、この洗浄時に
プロペラ11を回転させて撹拌し洗浄効果を高め
る。微粒子及び不純物を含む洗浄液12は、ポン
プ2の作用により液入口部8を通つて第1及び第
2の過装置3,4に流入する。第1の過装置
3においては5μ以上の、又第2の過装置4に
おいては1μ〜5μの微粒子及び不純物がそれぞれ
除去され、このようにして清浄化された洗浄液1
2は、液出口部9を通つて浴槽7内に戻される。
このように洗浄液12を循環使用しながら石油ピ
ツチ活性炭13が十分に洗浄される。
この洗浄方法において、洗浄条件は活性炭の性
質、装置の特性、規模などにより異なるが、通常
1Kgの石油ピツチ活性炭を洗浄する場合、流速
0.5〜5.0/minで1〜4時間程度おこない、洗
浄液中の2μ以上の微粒子の数を100個/ml以下、
5μ以上の微粒子の数を0個/mlと清浄化する。
このようにして十分超音波洗浄された石油ピツ
チ活性炭13を数回デカンテーシヨン洗浄をくり
返した後第2図に示すようにカラム14に充填し
オートクレーブ滅菌をおこなうことにより、人工
肝、人工腎補助用の血液浄化装置が得られる。こ
の装置は血液中に含まれるクレアチニン、イヌリ
ン、農薬、睡眠剤等の中分子の毒物や有機物を活
性炭13に吸着させてこれを除去する作用を有す
る。この場合石油ピツチ活性炭13には、微粒
子、不純物が剥離除去されているので、ここに血
小板等の血球がほとんど付着せず、又微粒子等が
生体に流出せず血栓の生成を防止でき、この結果
その生体適合性をコーテイングした従来のものと
同様とすることができる。しかもコーテイングし
てないので吸着能が高く装置の小型化を図れ、又
コーテイングによる有機溶剤の残留、コーテイン
グ剤の溶出といつた問題を解消できる。
また石油ピツチ活性炭は、従来から抗血栓材料
として評価されているグラフアイトと同様なもの
で、その観点からしても石油ピツチ活性炭をコー
テイングしないでそのまま用いることが有利であ
る。
なお本発明において石油ピツチ活性炭を用い、
ヤシガラ活性炭を用いなかつたのは次の理由によ
る。すなわちヤシガラ活性炭は、表面の凹凸が激
しく多くの微粒子を含んでおり、硬度が低く超音
波洗浄によりこれを剥離除去することは実際上不
可能であるのに対し、石油ピツチ活性炭は表面形
状が円滑で、微粒子も少なく硬度が高いので、超
音波洗浄によりこれを容易に剥離除去できる為で
ある。
なお上記実施例では、2μと5μのカートリツジ
フイルタを用いて微粒子を除去したが、本発明は
この組合せに限定するものではなく、又カートリ
ツジフイルタの個数もこれに限定するものではな
い。さらに過装置は、カートリツジフイルタに
限らず逆浸透装置、限外過装置など微粒子や不
純物を取り除けるものであればよい。
さらにまた石油ピツチ活性炭を充填したカラム
は、血液洗浄用に限らず、例えば人工腎用血液
過装置で分離された液の浄化用に用いることも
できる。
次に本発明方法の実施例を説明する。
第1図に示す洗浄装置において、超音波洗浄機
として超音波工業株式会社製のソリツド・ステイ
ト(Solid state)600を用い、過装置として立
石過株式会社製のカートリツジフイルタ(1μ
及び5μ)を用い、この超音波洗浄機に石油ピツ
チ活性炭(BAC−MU−ND−LE、クレハ化学
株式会社製、商標名)1Kgを入れ、無菌な生理食
塩液を加え、流速3/minで3時間連続して洗
浄した。この洗浄操作終了後各カートリツジフイ
ルタをそれぞれ観察したところ、遊出した微粒子
により黒変し、ここで微粒子を捕獲していること
が確認された。また液出口部から流出してくる生
理食塩液の微粒子の数をコールターカウンター
(コールターエレクトロニクス、インコーポレー
テイド社製、ZB型)で測定した結果2μ以上の微
粒子が100個/ml以下、5μ以上のものが0個/ml
と清浄であつた。
また洗浄前のものと洗浄後の活性炭表面を走査
型電子顕微鏡写真で調べた結果、洗浄前のものは
第3図に示すように微粒子が多数散在するが、洗
浄後のものは第4図に示すように微粒子は見られ
ず、十分洗浄できたことが認められた。
このようにして洗浄した石油ピツチ活性炭100
gをカラムに充填してオートクレーブ滅菌をおこ
なつた。この後このカラムに細孔メンブランフイ
ルター(0.22μ)で2回過した清浄な生理食塩
液を流速200ml/minで流し、5分後に流出して
きた生理食塩液中の微粒子をコールターカウンタ
ーで測定し、その結果を第1表に示す。
次に24〜28Kgの雑犬の頚動静脈にAVシヤント
を作成して全身へパリン化し、人工腎臓用血液循
環回路を形成して、この回路に上記カラムを接続
し、体外循環実験を行つた。
そして体外循環実験中の血小板の数の変動を測
定し、その結果を第5図のグラフに折線a1で示
す。またオートクレーブ滅菌済みの石油ピツチ活
性炭100gを充填した上記カラムに、ビタミン
B1220mg/dlの溶液を200ml/minの流速でシング
ルパスで流した。このときのクリアランスKTの
変化を測定し、その結果を第6図のグラフに折線
a2で示す。なおクリアランスKTは下式で示され
る。
TT=Ci−C0/Ci×QB
ただしKT:クリアランス(ml/min)
Ci:カラム入口濃度(mg%)
C0:カラム出口濃度(〃)
QB:液流速(ml/min)
比較例
コーテイング剤としてポリ−ハイドロキシエチ
ルメタクリレートを用い、このコーテイング剤15
gをエタノール2に投入して、加温溶解した後
ここに石油ピツチ活性炭1Kgを入れて温風下でエ
タノールを蒸発させた。次いで溶液がなくなつた
後90℃のオーブンに2日間放置し、コーテイング
した石油ピツチ活性炭を作製した。
このようにして得られた活性炭100gを実施例
と同様にカラムに充填してオートクレーブ滅菌を
行ない、この後生理食塩液を流して液中の微粒子
を測定し、その結果を第1表に併記する。又上記
実施例で洗浄しない石油ピツチ活性炭についても
同様の実験をおこない、その結果を第1表に併記
する。
さらにコーテイングした石油ピツチ活性炭を充
填したカラム及び洗浄しない石油ピツチ活性炭を
充填したカラムを用いて上記実施例と同じ体外循
環実験を行ない、その結果を第5図に折線b1(コ
ーテイングしたもの)及び折線C(洗浄しないも
の)で示す。また実施例と同じ実験条件でコーテ
イングしたものにつきクリアランスの変化を測定
し、その結果を第6図に折線b2で示す。
The present invention relates to a method for cleaning activated carbon for body fluid purification, which is used as it is without coating for use in artificial livers, artificial kidneys, etc. Conventionally, the activated carbon used in DHP columns for assisting artificial livers and artificial kidneys are coconut shell activated carbon and petroleum pitch activated carbon, but in most cases, this is not used as is, but the activated carbon is coated with collodion, hydrogel, cellulose, etc. on the surface. It is coated with a polymer membrane. The reason for coating is
This is to prevent fine particles (coal dust) from escaping from the activated carbon, as well as to prevent the adhesion of blood cells and the formation of blood clots caused by the fine particles, thereby imparting biocompatibility to the activated carbon. However, coated activated carbon has a low adsorption capacity because its surface is covered with a polymer film, and as a result, the amount of activated carbon used is large, making the device larger, and as a result, the amount of priming is large, making it difficult to perform extracorporeal circulation It places a heavy burden on patients and poses safety problems. Moreover, some organic solvent used during coating remains on the coated activated carbon, and the coating agent may be eluted during autoclave sterilization or long-term storage, which may have an adverse effect on living organisms. Apart from these, there is also a method in which uncoated coconut shell activated carbon is adhered to a tape to prevent the escape of fine particles. Since this product is not coated, it has a high adsorption capacity, but the equipment is complicated and the cost is high.Furthermore, since it uses an adhesive, there is a risk that impurities may be eluted from the adhesive when it comes into contact with blood. As described above, all conventional activated carbons for blood purification have problems with adsorption ability or biocompatibility. Therefore, the inventor conducted research to solve these problems, and as a result found the following. In other words, among activated carbons, coconut shell activated carbon has a very uneven surface and an extremely large amount of fine particles, but compared to this, oil pitch activated carbon has a smooth surface and a small amount of fine particles, and this activated carbon can be washed thoroughly. It was found that when the fine particles were peeled off and removed, there was no problem with biocompatibility even if the particles were used as they were without coating. The present invention has been made based on such knowledge, and it is possible to use activated carbon as it is without coating it to efficiently clean body fluids by effectively utilizing the cleaning liquid. The present invention provides a method for cleaning activated carbon for purification. That is, in the present invention, when cleaning petroleum pitch activated carbon with an ultrasonic cleaning machine to peel off and remove fine particles attached to the petroleum pitch activated carbon, a cleaning solution containing the fine particles removed from the petroleum pitch activated carbon with the cleaning machine is first washed. A step of filtering the fine particles to a predetermined size using a second filtering device, a step of further filtering the fine particles to a smaller size using a second filtering device, and a step of cleaning the fine particles in the first and second filtration steps. This method of cleaning activated carbon for body fluid purification is characterized by comprising a step of returning the cleaning liquid to the cleaning machine for circulation use. The present invention also provides an ultrasonic cleaning machine capable of storing a cleaning liquid and petroleum pitch activated carbon to be cleaned, and further having ultrasonic transmitting means, a cleaning liquid circulation circuit that communicates with the inside of the cleaning machine and circulates the cleaning liquid, and a cleaning liquid circulation circuit that communicates with the inside of the cleaning machine and circulates the cleaning liquid. a first filtration device that communicates with the inside of the circuit and filters particles contained in the cleaning solution to a predetermined size; and a second filtration device that further filters the particles to a smaller size. This is an activated carbon cleaning device for body fluid purification characterized by comprising a filtration device. The method and apparatus of the present invention will now be described with reference to illustrative embodiments. Figure 1 is an explanatory diagram showing the cleaning equipment used in this method. A cleaning liquid circulation path 5 is formed in. The ultrasonic cleaning machine 1 has a liquid inlet section 8 with a mesh and a liquid outlet section 9 of the cleaning liquid circulation path 5 disposed in a bathtub 7 equipped with an ultrasonic vibrator 6, and further has a stirring section driven by a motor 10. A propeller 11 is provided. This bath layer 7 is filled with a cleaning liquid 12 such as physiological saline, distilled water, dextran, etc., and petroleum pit activated carbon 13 is placed therein. The activated carbon 13 is preferably one that has high purity and hardness, and has few stray particles. Also, the first passing device 3 is
It is equipped with a 5μ cartridge filter, and the second filter device 4 is equipped with a 1μ cartridge filter. In this cleaning device, the ultrasonic vibrator 6 is operated to remove and clean fine particles and impurities adhering to the oil pit activated carbon 13, and during this cleaning, the propeller 11 is rotated to stir and improve the cleaning effect. The cleaning liquid 12 containing particulates and impurities flows into the first and second filtration devices 3 and 4 through the liquid inlet 8 by the action of the pump 2 . In the first filtration device 3, fine particles and impurities of 5μ or more are removed, and in the second filtration device 4, fine particles and impurities of 1μ to 5μ are removed, and the thus cleaned cleaning liquid 1
2 is returned into the bathtub 7 through the liquid outlet section 9.
In this way, the petroleum pit activated carbon 13 is thoroughly washed while using the cleaning liquid 12 in circulation. In this cleaning method, the cleaning conditions vary depending on the properties of the activated carbon, characteristics of the equipment, scale, etc., but normally when cleaning 1 kg of petroleum pitch activated carbon, the flow rate is
Run at 0.5 to 5.0/min for about 1 to 4 hours to reduce the number of particles of 2μ or more in the cleaning solution to 100 particles/ml or less.
Purify the number of particles with a size of 5μ or more to 0/ml. After repeating decantation washing several times, the petroleum pit activated carbon 13 that has been thoroughly ultrasonically cleaned in this manner is filled into a column 14 as shown in Fig. 2, and sterilized in an autoclave to produce an artificial liver and an artificial kidney. A blood purification device for use is obtained. This device has the function of removing middle-molecular poisons and organic substances contained in the blood, such as creatinine, inulin, agricultural chemicals, and sleeping pills, by adsorbing them onto the activated carbon 13. In this case, since fine particles and impurities have been peeled off and removed from the petroleum pitch activated carbon 13, blood cells such as platelets hardly adhere thereto, and the fine particles do not flow into the living body, preventing the formation of blood clots. Its biocompatibility can be similar to that of conventional coatings. Moreover, since it is not coated, the adsorption capacity is high and the device can be miniaturized, and problems such as residual organic solvent and elution of the coating agent due to coating can be solved. Furthermore, petroleum pitch activated carbon is similar to graphite, which has been evaluated as an antithrombotic material, and from this point of view, it is advantageous to use petroleum pitch activated carbon as it is without coating. In addition, in the present invention, petroleum pitch activated carbon is used,
The reason why coconut shell activated carbon was not used is as follows. In other words, coconut shell activated carbon has a highly uneven surface and contains many fine particles, and its hardness is so low that it is practically impossible to remove it by ultrasonic cleaning, whereas oil pitch activated carbon has a smooth surface. This is because there are few fine particles and the hardness is high, so they can be easily peeled off and removed by ultrasonic cleaning. In the above embodiment, fine particles were removed using 2μ and 5μ cartridge filters, but the present invention is not limited to this combination, nor is the number of cartridge filters to be limited to this. Furthermore, the filtration device is not limited to a cartridge filter, but may be any device capable of removing particulates and impurities, such as a reverse osmosis device or an ultrafiltration device. Furthermore, the column filled with petroleum pit activated carbon can be used not only for blood washing but also for purifying the liquid separated by, for example, a blood filtering device for an artificial kidney. Next, examples of the method of the present invention will be described. In the cleaning apparatus shown in Fig. 1, a Solid State 600 manufactured by Ultrasonic Industries Co., Ltd. is used as an ultrasonic cleaning machine, and a cartridge filter (1μ
and 5 μ), put 1 kg of petroleum pitch activated carbon (BAC-MU-ND-LE, manufactured by Kureha Chemical Co., Ltd., trade name) into this ultrasonic cleaner, add sterile physiological saline solution, and wash at a flow rate of 3/min. Washed continuously for 3 hours. When each cartridge filter was observed after completing this cleaning operation, it was found that the filters turned black due to the escaped particles, and it was confirmed that the particles were captured there. In addition, the number of particles in the physiological saline flowing out from the liquid outlet was measured using a Coulter counter (Model ZB, manufactured by Coulter Electronics, Incorporated).The results showed that the number of particles larger than 2μ was less than 100 particles/ml, and the number of particles larger than 5μ was 100 particles/ml. 0 pieces/ml
It was clean and warm. Furthermore, as a result of scanning electron micrographs of the activated carbon surface before and after cleaning, it was found that many fine particles were scattered on the surface of the activated carbon before cleaning, as shown in Figure 3, while that of the activated carbon after cleaning was shown in Figure 4. As shown, no fine particles were observed, indicating that sufficient cleaning was possible. Petroleum pitch activated carbon 100 washed in this way
g was packed into a column and sterilized in an autoclave. After that, a clean physiological saline solution that had been passed twice through a pore membrane filter (0.22μ) was flowed through this column at a flow rate of 200 ml/min, and after 5 minutes, the particles in the physiological saline solution that had flowed out were measured using a Coulter counter. The results are shown in Table 1. Next, an AV shunt was created in the carotid artery and vein of a 24-28 kg mongrel dog, and the whole body was heparinized to form a blood circulation circuit for an artificial kidney.The above column was connected to this circuit, and an extracorporeal circulation experiment was performed. . Fluctuations in the number of platelets during the extracorporeal circulation experiment were measured, and the results are shown in the graph of FIG. 5 by broken line a1 . In addition, vitamin
A solution of 20 mg/dl B 12 was flowed in a single pass at a flow rate of 200 ml/min. Measure the change in clearance K T at this time, and plot the results as a broken line in the graph of Figure 6.
Indicated by a 2 . The clearance K T is expressed by the formula below. T T = C i − C 0 / C i ×Q B where K T : Clearance (ml/min) C i : Column inlet concentration (mg%) C 0 : Column outlet concentration (〃) Q B : Liquid flow rate (ml /min) Comparative Example Using poly-hydroxyethyl methacrylate as a coating agent, this coating agent 15
After putting 1 kg of petroleum pitch activated carbon into 2 ml of ethanol and dissolving it by heating, 1 kg of petroleum pitch activated carbon was added and the ethanol was evaporated under hot air. After the solution had run out, the mixture was left in an oven at 90°C for 2 days to produce coated petroleum pit activated carbon. 100 g of the activated carbon thus obtained was packed into a column and sterilized in an autoclave in the same manner as in the example. After that, a physiological saline solution was poured in to measure the particulates in the solution, and the results are also listed in Table 1. . Similar experiments were also conducted using petroleum pit activated carbon that was not washed in the above example, and the results are also shown in Table 1. Furthermore, the same extracorporeal circulation experiment as in the above example was conducted using a column packed with coated petroleum pit activated carbon and a column packed with unwashed petroleum pitch activated carbon. It is shown by broken line C (not washed). Further, the change in clearance was measured for the coated material under the same experimental conditions as in the example, and the results are shown in FIG. 6 by broken line b2 .
【表】
第1表及び第5図から本発明方法に係る石油ピ
ツチ活性炭は、これをコーテイングせずにそのま
ま用いても微粒子が遊出せず又血小板の減少も少
なく、生体適合性の点で従来のコーテイングした
ものと、なんら遜色がないことが確認された。
また第6図に示す実験結果から本発明方法に係
る石油ピツチ活性炭を用いれば、コーテイングし
たものに比べてクリアランスを高く維持でき、吸
着能が約2倍と極めて向上することが認められ
た。
以上説明したように本発明方法によれば、コー
テイングしないで用いる為の石油ピツチ活性炭を
効率よくしかも洗浄液を有効に利用して洗浄する
ことができる。しかもこの方法で得られた石油ピ
ツチ活性炭は、コーテイングしないで用いるので
吸着能が高く装置を小型化でき、小型化に併つて
プライミング量が少なくなり、体外循環時の患者
への負担を軽くできる。またコーテイングによる
有機溶剤の残留、コーテイング剤の溶出の問題を
解消でき、さらには、活性炭の使用量が少ないの
でコストの軽減を図れ、コーテイング操作がない
ので生産工程が少なく、製作が容易となるなど
種々の顕著な効果を奏する。さらに、本発明の装
置によれば、上記効果を有する本発明の方法を確
実かつ容易に行うことができる。[Table] From Table 1 and Fig. 5, the petroleum pit activated carbon according to the method of the present invention does not release fine particles or cause a small decrease in platelets even when used as it is without coating, and is superior to conventional methods in terms of biocompatibility. It was confirmed that there was no inferiority to that coated with . Furthermore, from the experimental results shown in FIG. 6, it was confirmed that by using the petroleum pit activated carbon according to the method of the present invention, the clearance could be maintained higher than that of the coated carbon, and the adsorption capacity was significantly improved to about twice that. As explained above, according to the method of the present invention, petroleum pitch activated carbon, which is used without coating, can be cleaned efficiently and by effectively utilizing the cleaning liquid. Moreover, since the petroleum pitch activated carbon obtained by this method is used without being coated, it has a high adsorption capacity and the device can be made smaller.As the device is made smaller, the amount of priming is reduced, and the burden on the patient during extracorporeal circulation can be reduced. In addition, the problem of organic solvent residue and coating agent elution due to coating can be solved.Furthermore, since the amount of activated carbon used is small, costs can be reduced, and since there is no coating operation, there are fewer production steps, making production easier. It has various remarkable effects. Furthermore, according to the apparatus of the present invention, the method of the present invention having the above effects can be carried out reliably and easily.
第1図は本発明方法に用いる洗浄装置の一実施
例を示した説明図、第2図は本発明方法で洗浄さ
れた石油ピツチ活性炭をカラム内に充填した状態
を示す概略断面図、第3図は洗浄前の石油ピツチ
活性炭を走査型電子顕微鏡で観察した顕微鏡写
真、第4図は洗浄後の石油ピツチ活性炭を走査型
電子顕微鏡で観察した顕微鏡写真、第5図は第2
図のカラムを用いて時間の経過による血小板の量
の変化を比較例のものとともに折線で示した特性
図、第6図は同カラムにおいて、時間の経過によ
るクリアランスの変化を比較例のものとともに折
線で示した特性図である。
1……超音波洗浄機、2……ポンプ、3……第
1の過装置、4……第2の過装置、12……
洗浄液、13……石油ピツチ活性炭、14……カ
ラム。
FIG. 1 is an explanatory diagram showing one embodiment of the cleaning device used in the method of the present invention, FIG. 2 is a schematic sectional view showing a column filled with petroleum pitch activated carbon cleaned by the method of the present invention, and FIG. The figure is a micrograph of petroleum pitch activated carbon observed before washing using a scanning electron microscope. Figure 4 is a micrograph of petroleum pitch activated carbon observed after washing using a scanning electron microscope.
Figure 6 is a characteristic diagram showing the changes in the amount of platelets over time using the same column as a broken line along with that of a comparative example. FIG. 1... Ultrasonic cleaner, 2... Pump, 3... First filtering device, 4... Second filtering device, 12...
Cleaning liquid, 13... Petroleum pitch activated carbon, 14... Column.
Claims (1)
該石油ピツチ活性炭に付着した微粒子を剥離除去
する際に、上記洗浄機で該石油ピツチ活性炭から
除去した微粒子を含む洗浄液を第1の濾過装置に
より微粒子を所定の大きさまで濾過する工程と、
第2の濾過装置でさらに該微粒子をより小さな大
きさのものまで濾過する工程と、第1及び第2の
濾過工程で清浄化された洗浄液を上記洗浄機に戻
して循環使用する工程とからなることを特徴とす
る体液浄化用活性炭の洗浄方法。 2 洗浄液及び洗浄される石油ピツチ活性炭を収
納でき、さらに超音波発信手段を有する超音波洗
浄機と、該洗浄機の内部に連通し洗浄液を循環さ
せる洗浄液循環回路と、該回路中に取付けられた
洗浄液循環用ポンプと、上記回路内と連通して洗
浄液に含まれる微粒子を所定の大きさまで濾過す
る第1の濾過装置と、更に該微粒子を、より小さ
な大きさまで濾過する第2の濾過装置とからなる
ことを特徴とする体液浄化用活性炭洗浄装置。[Scope of Claims] 1. When cleaning petroleum pit activated carbon with an ultrasonic cleaner to peel off and remove fine particles attached to the petroleum pitch activated carbon, a cleaning solution containing the fine particles removed from the petroleum pitch activated carbon with the cleaning machine is used. a step of filtering fine particles to a predetermined size using a first filtration device;
It consists of a step of further filtering the fine particles to smaller particles in a second filtration device, and a step of returning the cleaning liquid cleaned in the first and second filtration steps to the washing machine for circulation use. A method for cleaning activated carbon for body fluid purification, characterized by: 2. An ultrasonic cleaning machine capable of storing cleaning liquid and petroleum pitch activated carbon to be cleaned, and further having ultrasonic transmitting means, a cleaning liquid circulation circuit that communicates with the interior of the cleaning machine and circulates the cleaning liquid, and an ultrasonic cleaning machine installed in the circuit. A cleaning liquid circulation pump, a first filtration device that communicates with the inside of the circuit and filters particulates contained in the cleaning liquid to a predetermined size, and a second filtration device that further filters the particulates to a smaller size. An activated carbon cleaning device for body fluid purification characterized by:
Priority Applications (12)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13946579A JPS5662540A (en) | 1979-10-29 | 1979-10-29 | Washing method of active carbon for purifying body fluid |
| US06/200,915 US4358376A (en) | 1979-10-29 | 1980-10-27 | Apparatus for detoxifying body fluid |
| CA000363428A CA1144484A (en) | 1979-10-29 | 1980-10-28 | Apparatus for detoxifying body fluid |
| BE0/202619A BE885911A (en) | 1979-10-29 | 1980-10-28 | APPARATUS FOR DETOXICATING A LIQUID FROM THE ORGANISM |
| AU64828/80A AU528671B2 (en) | 1979-10-29 | 1980-10-29 | Body fluid-purifying apparatus |
| DE19803049976 DE3049976A1 (en) | 1979-10-29 | 1980-10-29 | BODY FLUID-PURIFYING APPARATUS |
| PCT/JP1980/000268 WO1981001103A1 (en) | 1979-10-29 | 1980-10-29 | Body fluid-purifying apparatus |
| NLAANVRAGE8020407,A NL185132C (en) | 1979-10-29 | 1980-10-29 | DEVICE FOR DETOXIFYING BODY FLUIDS. |
| IT25638/80A IT1134090B (en) | 1979-10-29 | 1980-10-29 | BODY FLUID DETOXIFICATION EQUIPMENT |
| GB8120004A GB2074168B (en) | 1979-10-29 | 1980-10-29 | Body fluid-purifying apparatus |
| EP80902124A EP0038860B1 (en) | 1979-10-29 | 1981-05-04 | Body fluid-purifying apparatus |
| SE8103926A SE445803B (en) | 1979-10-29 | 1981-06-23 | DEVICE CONTAINING ACTIVE COAL FOR THE DETECTION OF A BODY LIQUID |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13946579A JPS5662540A (en) | 1979-10-29 | 1979-10-29 | Washing method of active carbon for purifying body fluid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5662540A JPS5662540A (en) | 1981-05-28 |
| JPS6341616B2 true JPS6341616B2 (en) | 1988-08-18 |
Family
ID=15245857
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13946579A Granted JPS5662540A (en) | 1979-10-29 | 1979-10-29 | Washing method of active carbon for purifying body fluid |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPS5662540A (en) |
| BE (1) | BE885911A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20010074185A (en) * | 2001-04-06 | 2001-08-04 | 김정술 | Activated Carbon Automatic Cleaning Method by Ultrasonic and High Frequency |
| CN1988926B (en) * | 2004-07-23 | 2010-05-05 | 株式会社钟化 | Adsorber for direct blood perfusion filled with adsorbent from which water-insoluble fine particles were removed, and method of obtaining adsorbent for direct blood perfusion from which water-insoluble fine particles were removed |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS525430B2 (en) * | 1973-10-09 | 1977-02-14 |
-
1979
- 1979-10-29 JP JP13946579A patent/JPS5662540A/en active Granted
-
1980
- 1980-10-28 BE BE0/202619A patent/BE885911A/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5662540A (en) | 1981-05-28 |
| BE885911A (en) | 1981-02-16 |
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