JPS649029B2 - - Google Patents
Info
- Publication number
- JPS649029B2 JPS649029B2 JP53110472A JP11047278A JPS649029B2 JP S649029 B2 JPS649029 B2 JP S649029B2 JP 53110472 A JP53110472 A JP 53110472A JP 11047278 A JP11047278 A JP 11047278A JP S649029 B2 JPS649029 B2 JP S649029B2
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- desorption
- urea
- toxic substances
- blood
- 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
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 46
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 27
- 239000004202 carbamide Substances 0.000 claims description 23
- 238000000034 method Methods 0.000 claims description 22
- 210000004369 blood Anatomy 0.000 claims description 18
- 239000008280 blood Substances 0.000 claims description 18
- 239000003440 toxic substance Substances 0.000 claims description 17
- 231100000614 poison Toxicity 0.000 claims description 16
- 239000000706 filtrate Substances 0.000 claims description 14
- 210000003734 kidney Anatomy 0.000 claims description 13
- 238000001179 sorption measurement Methods 0.000 claims description 13
- 238000000108 ultra-filtration Methods 0.000 claims description 12
- 239000003463 adsorbent Substances 0.000 claims description 11
- 229920002239 polyacrylonitrile Polymers 0.000 claims description 11
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 10
- 239000012528 membrane Substances 0.000 claims description 8
- 210000001367 artery Anatomy 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 6
- 239000000835 fiber Substances 0.000 claims description 5
- 210000003462 vein Anatomy 0.000 claims description 5
- 239000002657 fibrous material Substances 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 231100000167 toxic agent Toxicity 0.000 claims 1
- 238000003795 desorption Methods 0.000 description 24
- DDRJAANPRJIHGJ-UHFFFAOYSA-N creatinine Chemical compound CN1CC(=O)NC1=N DDRJAANPRJIHGJ-UHFFFAOYSA-N 0.000 description 14
- 229940109239 creatinine Drugs 0.000 description 7
- LEHOTFFKMJEONL-UHFFFAOYSA-N Uric Acid Chemical compound N1C(=O)NC(=O)C2=C1NC(=O)N2 LEHOTFFKMJEONL-UHFFFAOYSA-N 0.000 description 6
- TVWHNULVHGKJHS-UHFFFAOYSA-N Uric acid Natural products N1C(=O)NC(=O)C2NC(=O)NC21 TVWHNULVHGKJHS-UHFFFAOYSA-N 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 6
- 229940116269 uric acid Drugs 0.000 description 6
- 238000000502 dialysis Methods 0.000 description 5
- 210000002966 serum Anatomy 0.000 description 5
- 229940045136 urea Drugs 0.000 description 4
- 239000000243 solution Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004480 active ingredient Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000002637 fluid replacement therapy Methods 0.000 description 2
- 238000001631 haemodialysis Methods 0.000 description 2
- 230000000322 hemodialysis Effects 0.000 description 2
- 208000037157 Azotemia Diseases 0.000 description 1
- 229920000298 Cellophane Polymers 0.000 description 1
- 206010070863 Toxicity to various agents Diseases 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000001684 chronic effect Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 208000017169 kidney disease Diseases 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 208000009852 uremia Diseases 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- External Artificial Organs (AREA)
Description
本発明は、限外濾過方式による人工腎臓装置に
おいて、濾過液中に含まれる尿素、尿酸、クレア
チニン等の有毒物質を除去する方法に関するもの
である。
近年、慢性尿毒症や急性腎臓疾患あるいは薬物
中毒に対して血液透析が広く採用され、人工腎臓
装置が欠くべからざるものとなつている。現在、
最も広く使われている人工腎臓装置は、主として
セロフアン透析膜と透析液とからなつており、透
析膜を介して患者動脈からの血液と透析液を流し
て、血液中の老廃物、たとえば尿素、尿酸、クレ
アチニンなどを血液と透析液中の濃度差を利用し
て、透析液中に移行せしめ、血液の浄化を行なつ
ている。
今日までの透析型人工腎臓装置では、一度透析
された透析液は、全て廃棄され、常に新しい透析
液を供給してやる必要があり、その透析液にかけ
る費用だけでも、非常に高額なものになつている
のが実情である。
透析法によると、先述した如く透析液を全て廃
棄するため、大量の水が必要となり、装置は大型
となり、よつて患者は上下水道の完備した病院の
ベツト等に長時間拘束されることになる。
また、限外濾過膜を用いて、血液より血清を分
離し、血液に含まれる有毒物質を血清とともに捨
て、その代りに補液を生体に注入する、いわゆる
濾過型人工腎臓装置がある。濾過型人工腎臓装置
においては、有用な成分を含む血清を廃棄しなく
てすむ方式の開発が待たれている。
透析、濾過以外の有効な方法としては、上記尿
素などの含窒素化合物を吸着する性質を有する活
性炭、アルミナ等の吸着剤を容器に詰めて、この
容器中を動脈からの血液を通過させることによ
り、含窒素化合物を吸着除去する方法がある。
活性炭素による吸着法は、上述の透析法に比べ
て、含窒素化合物の除去能力は、格段に優れてい
る。しかしながら、この吸着法によれば、含窒素
化合物のうち尿酸、クレアチニンは比較的容易に
吸着されるが、尿素が吸着される量は比較的少な
いので、かなり大量の吸着剤を必要とする。ま
た、血液が吸着剤に直接触れると、血液中の有効
成分も吸着してしまうという大きな欠点を持つて
いる。
本発明者らは、上記のような血液透析法、濾過
法および吸着法の欠点を克服し、また、それらの
方法が持つ利点を有効に利用すべく鋭意検討した
結果、限外濾過法と活性炭による吸着法を併用
し、しかも、活性炭としてポリアクリロニトリル
繊維を原料とした含窒素繊維状活性炭を選用し、
加えて吸着剤の吸脱着を交互または輪番的に行な
わしめることが非常に有効であることを見出し
た。
本発明は、限外濾過方式による人工腎臓装置に
おいて動脈からの血液を限外濾過膜で濾過した濾
過液中に含まれる尿素等の有毒物質を除去するに
当り、ポリアクリロニトリル繊維を原料とした含
窒素繊維状活性炭吸着剤を充填した2個または2
個以上の吸着器を交互または輪番的に用い、1個
またはそれ以上の吸着器では有毒物質の吸着を行
ない、その間に、吸着に利用されていない吸着ず
みの吸着器では有毒物質の脱着を行ない、再生濾
過液を静脈に戻すことを特徴とする人工腎臓装置
における有毒物質の除去方法である。
以下に本発明について詳述する。患者の動脈か
らの血液を、まず限外濾過装置に導入し、濾過さ
れた尿素、尿酸、クレアチニン等を含む濾過液は
次のポリアクリロニトリル系繊維状活性炭吸着装
置へと導く。患者の濾過されなかつた血液は、そ
のまま患者の体内に戻すか、または、有毒物質を
吸着除去した浄化血清と混合したのち患者の静脈
に戻す。尿素等を含んだ濾過液は、繊維状活性炭
吸着器へと導き、尿素、尿酸、クレアチニン等の
有毒物質を吸着除去する。繊維状活性炭吸着器
は、2個または2個以上を用い、吸着剤層を通過
する濾過液と脱着用水溶液の流れを自動切換装置
によつてコントロールする。すなわち、ある吸着
器で濾過液中の有毒物質を吸着除去している間
に、他の吸着器では、脱着を行なわしめている。
吸着器は本方式の場合3器が好ましい。2器で吸
着を行なつている間に1器で脱着する組合わせ構
成が、時間等の効率から、もつとも好ましい。脱
着用水溶液については、血清の電解質濃度がうす
まるのを防ぐため、補液に相当する水溶液を用い
る。しかし、脱着プロセスの初期には水を利用す
ることも可能である。
人体から排泄しなければならない尿素は非常に
多量である。しかし、先述した如く、活性炭は尿
素の吸着に関しては、短時間で飽和点に達してし
まうという欠点を有している。ゆえに、尿素を除
くためには、大量の活性炭が必要となつてくる。
この問題を解決するため、本発明者らは、前述し
た如く、ポリアクリロニトリル系繊維状活性炭を
用い、これを再生しながら吸着する方法を採用し
た。
本発明の方法によると、吸着剤との接触を短か
くすることができ、有効成分の除去を避けること
が可能である。
本発明では、少量の繊維状活性炭で短時間で吸
脱着を繰返すことによつて、吸着器の活性炭量は
少量ですますことができるので、人工腎臓装置
は、大幅に小型化することができ、状況によつて
は携帯可能の装置にすることができる。
本発明では、ポリアクリロニトリル繊維を原料
とした含窒素繊維状活性炭が使用される。このも
のは、尿素の吸脱着、とりわけ脱着の性能が優れ
ているので、人工腎臓装置をより小型化すること
ができる。
本発明で使用されるところのポリアクリロニト
リル繊維を原料とした含窒素繊維状活性炭は、特
開昭51−137694号公報に記載された方法等によつ
て得られるものである。
本発明によると、限外濾過膜によつて得られた
濾過液から、有毒物質のみを吸着除去して、再び
体内に戻すため、従来一部に行なわれている濾過
方式人工腎臓のような血清廃棄に伴う補液の必要
がなく、非常に合理的なシステムとなつている。
本発明の方法においては、第1図に例示するよ
うな方式が用いられる。この系統図に従つて、本
発明をより詳細に説明する。
患者の動脈から導かれた血液は、管1から限外
濾過器3に入り、管2を経て患者の静脈に戻る。
一方、限外濾過器3の限外濾過膜4で濾過された
濾過液は、管5に導かれ、ポンプ6により、繊維
状活性炭吸着器7に入る。同吸着器7を出た濾過
液は、管8を通つて、管2の血液と合流させ、必
要ならば電解液を調整し患者の静脈に戻る。繊維
状活性炭吸着器の脱着については、脱着水溶液入
口9から入つてきた脱着用水溶液は、ポンプ10
で繊維状活性炭吸着器7に導かれ、有毒物を脱着
したあと、その有毒物を含む脱着用水溶液は、脱
着用水溶液出口11から廃棄される。
本発明が、従来法に比較して優れていること
は、下記の実験例からも明らかである。
患者の動脈から採取した血液は、まず限外濾過
装置に通し、得られた濾過液について含まれてい
る尿素の吸着、脱着実験を行なつた。第一表にそ
の結果を示す。
The present invention relates to a method for removing toxic substances such as urea, uric acid, and creatinine contained in a filtrate in an ultrafiltration artificial kidney device. In recent years, hemodialysis has been widely adopted for chronic uremia, acute kidney disease, or drug poisoning, and artificial kidney devices have become indispensable. the current,
The most widely used artificial kidney device mainly consists of a cellophane dialysis membrane and a dialysate. Blood from the patient's artery and the dialysate flow through the dialysis membrane to remove waste products in the blood, such as urea, Uric acid, creatinine, etc. are transferred into the dialysate by utilizing the difference in concentration between the blood and the dialysate to purify the blood. In the dialysis-type artificial kidney machines to date, once the dialysate has been dialyzed, all the dialysate is discarded, and new dialysate must be constantly supplied, and the cost alone for the dialysate becomes extremely expensive. The reality is that there are. According to the dialysis method, as mentioned above, all the dialysate is discarded, which requires a large amount of water, the equipment is large, and the patient is confined for a long time in a bed in a hospital equipped with water and sewage systems. . There is also a so-called filtration type artificial kidney device that uses an ultrafiltration membrane to separate serum from blood, discard toxic substances contained in the blood along with the serum, and inject replacement fluid into the living body instead. In filtration-type artificial kidney devices, the development of a method that eliminates the need to discard serum containing useful components is awaited. An effective method other than dialysis and filtration is to fill a container with an adsorbent such as activated carbon or alumina that has the property of adsorbing nitrogen-containing compounds such as urea, and allow blood from the artery to pass through the container. There is a method of adsorbing and removing nitrogen-containing compounds. The adsorption method using activated carbon has a much better ability to remove nitrogen-containing compounds than the above-mentioned dialysis method. However, according to this adsorption method, among nitrogen-containing compounds, uric acid and creatinine are adsorbed relatively easily, but the amount of urea adsorbed is relatively small, so a fairly large amount of adsorbent is required. Another major drawback is that when blood comes into direct contact with the adsorbent, the active ingredients in the blood are also adsorbed. The inventors of the present invention have conducted intensive studies to overcome the drawbacks of hemodialysis, filtration, and adsorption methods as described above, and to effectively utilize the advantages of these methods. In addition, nitrogen-containing fibrous activated carbon made from polyacrylonitrile fibers was selected as the activated carbon.
In addition, we have found that it is very effective to adsorb and desorb the adsorbent alternately or in a rotating manner. The present invention provides a method for removing toxic substances such as urea contained in the filtrate obtained by filtering blood from an artery through an ultrafiltration membrane in an artificial kidney device using an ultrafiltration method. 2 or 2 filled with nitrogen fibrous activated carbon adsorbent
One or more adsorbers are used alternately or in rotation, with one or more adsorbers adsorbing toxic substances, while the adsorbed adsorbers not being used for adsorption desorb toxic substances. , a method for removing toxic substances in an artificial kidney device, characterized by returning the regenerated filtrate to the vein. The present invention will be explained in detail below. Blood from the patient's artery is first introduced into an ultrafiltration device, and the filtered filtrate containing urea, uric acid, creatinine, etc. is led to the next polyacrylonitrile-based fibrous activated carbon adsorption device. The patient's unfiltered blood is either returned to the patient's body as is, or mixed with purified serum from which toxic substances have been adsorbed and then returned to the patient's veins. The filtrate containing urea and the like is guided to a fibrous activated carbon adsorber, where toxic substances such as urea, uric acid, and creatinine are adsorbed and removed. Two or more fibrous activated carbon adsorbers are used, and the flow of the filtrate and desorption aqueous solution passing through the adsorbent layer is controlled by an automatic switching device. That is, while one adsorber is adsorbing and removing toxic substances from the filtrate, another adsorber is desorbing them.
In the case of this method, it is preferable to use three adsorbers. A combination configuration in which adsorption is performed in two devices and desorption is performed in one device is most preferable from the viewpoint of efficiency in terms of time and the like. As for the aqueous solution for desorption, an aqueous solution equivalent to a replacement fluid is used to prevent the electrolyte concentration of serum from diluting. However, it is also possible to use water at the beginning of the desorption process. The amount of urea that must be excreted from the human body is very large. However, as mentioned above, activated carbon has the disadvantage that it reaches a saturation point in a short period of time when adsorbing urea. Therefore, a large amount of activated carbon is required to remove urea.
In order to solve this problem, the present inventors adopted a method of adsorbing while regenerating polyacrylonitrile-based fibrous activated carbon, as described above. According to the method of the invention, the contact with the adsorbent can be shortened and removal of the active ingredient can be avoided. In the present invention, by repeating adsorption and desorption using a small amount of fibrous activated carbon in a short period of time, the amount of activated carbon in the adsorber can be reduced to a small amount, so the artificial kidney device can be significantly downsized. Depending on the situation, it can be a portable device. In the present invention, nitrogen-containing fibrous activated carbon made from polyacrylonitrile fibers is used. This device has excellent adsorption and desorption performance of urea, especially in desorption performance, so that the artificial kidney device can be made more compact. The nitrogen-containing fibrous activated carbon made from polyacrylonitrile fibers used in the present invention is obtained by the method described in JP-A-51-137694. According to the present invention, only toxic substances are adsorbed and removed from the filtrate obtained by the ultrafiltration membrane, and then returned to the body. There is no need for fluid replacement upon disposal, making it a very rational system. In the method of the present invention, a system as illustrated in FIG. 1 is used. The present invention will be explained in more detail according to this system diagram. Blood directed from the patient's artery enters the ultrafilter 3 through tube 1 and returns via tube 2 to the patient's vein.
On the other hand, the filtrate filtered through the ultrafiltration membrane 4 of the ultrafilter 3 is led to a pipe 5 and enters the fibrous activated carbon adsorbent 7 by a pump 6. The filtrate leaving the adsorbent 7 passes through a tube 8, merges with the blood in the tube 2, adjusts the electrolyte if necessary, and returns to the patient's vein. For desorption of the fibrous activated carbon adsorber, the aqueous desorption solution entering from the desorption aqueous solution inlet 9 is pumped through the pump 10.
After being led to the fibrous activated carbon adsorber 7 and desorbing the toxic substances, the aqueous desorption solution containing the toxic substances is discarded from the aqueous desorption solution outlet 11. It is clear from the following experimental examples that the present invention is superior to conventional methods. Blood taken from the patient's artery was first passed through an ultrafiltration device, and the resulting filtrate was subjected to adsorption and desorption experiments for the urea contained therein. Table 1 shows the results.
【表】
第一表の下段「脱着」の横欄をみると、脱着時
初濃度0が3分(min)後に早くも32.3mg%にな
り、これが30分間にわたり実質上維持されてい
る。
このことは、脱着時濃度が僅か3分で平衡に達
し、脱着が有効に行なわれたことを意味し、これ
によれば、含窒素繊維状活性炭を用いた場合に、
尿素の脱着が極めて短時間で容易かつ有効に行な
われたことがわかる。
本発明では、ポリアクリロニトリル繊維を原料
とした含窒素繊維状活性炭(PAN系ACF)が使
用されるが、本発明は、一般に用いられている活
性炭(AC)の場合に比較し、尿素、尿酸、クリ
アチニン等の有害物質の吸脱着効果において優れ
ている。
ACでもACFにおいても、尿素は一般に吸着さ
れにくく容易に飽和になるが、前記のように、
PAN系ACFの場合、尿素に対する脱着が容易で
あり、脱着し再生したACFは、繰返し使用する
ことができる。しかも、PAN系ACFは、再生処
理が短時間ですむことから使用量が少量ですみ、
短時間で吸脱着できるので、本発明方法を適用し
た装置は、小型化、簡便型化が可能である。
一方、ACの場合は、吸着に関してはPAN系
ACFと同じであるが、脱着速度が遅いことが欠
点で、再生利用に適していない。使用ずみACは
通常廃棄されるが、強いて再生利用しようとする
と相当大きな装置が必要となる。
ACを用いた場合における尿素の脱着に関する
比較実験結果は、第二表に示すとおりである。[Table] Looking at the column next to "Desorption" at the bottom of Table 1, the initial concentration at the time of desorption is 0, but after 3 minutes (min) it reaches 32.3 mg%, and this is essentially maintained for 30 minutes. This means that the concentration during desorption reached equilibrium in just 3 minutes, and desorption was carried out effectively.According to this, when nitrogen-containing fibrous activated carbon was used,
It can be seen that urea was easily and effectively desorbed in an extremely short period of time. In the present invention, nitrogen-containing fibrous activated carbon (PAN-based ACF) made from polyacrylonitrile fibers is used. It has excellent adsorption and desorption effects for harmful substances such as creatinine. In both AC and ACF, urea is generally difficult to adsorb and easily becomes saturated, but as mentioned above,
In the case of PAN-based ACF, it is easy to desorb urea, and the desorbed and regenerated ACF can be used repeatedly. Moreover, PAN-based ACF can be recycled in a short time, so only a small amount of it can be used.
Since adsorption and desorption can be carried out in a short time, the device to which the method of the present invention is applied can be made smaller and simpler. On the other hand, in the case of AC, PAN-based
It is the same as ACF, but its drawback is that it has a slow desorption speed, making it unsuitable for recycling. Used ACs are normally disposed of, but if you try to recycle them, you will need a fairly large piece of equipment. Comparative experimental results regarding urea desorption using AC are shown in Table 2.
【表】
この第二表の結果によれば、ACを用いた場合
には、脱着時濃度が32.3mg%に達するに要した時
間は30分であり、これを前記第一表のPAN系
ACFを用いた場合に、同じ32.3mg%に達するに要
した時間の3分に比較すると、ACを用いた場合
の所要時間は、実に10倍も長いことになる。
本発明の効果を要約すると、次のとおりであ
る。第一表の結果から明らかなように、本発明に
よつて、血中尿素量を当初の約3/4に低下させる
ことができる(換言すれば、吸着されて除去され
た尿素量が当初の約1/4、そして、吸着されずに
残存した尿素量が当初の約3/4となる。)。尿素量
をこの程度低下させれば、濾過液を再び人体の血
液中に戻しても、何ら問題を生じることがないの
である。
本発明によると、限外濾過方式と繊維状活性炭
吸着剤を組合わせることによつて、尿素、尿酸、
クレアチニンなどの有毒物質を効果的に除去でき
るとともに、処置時間を大きく短縮させ、長時間
使用も可能となる。本発明によると、装置を小型
携帯用にすることができ、加えて透析液を用いる
必要もなく、また補液の必要もないので、かなり
安価である。
本発明の方法によつて、従来の濾過型人工腎臓
の最大の欠点であつた物質収支がとれないという
問題が解消されたわけで、この点だけをとつてみ
ても、本発明は画期的なものといえる。[Table] According to the results in Table 2, when AC was used, the time required to reach a concentration of 32.3 mg% during desorption was 30 minutes.
Compared to the 3 minutes required to reach the same 32.3 mg% using ACF, the time required using AC is actually 10 times longer. The effects of the present invention can be summarized as follows. As is clear from the results in Table 1, the present invention can reduce the amount of urea in the blood to approximately 3/4 of the initial amount (in other words, the amount of urea adsorbed and removed is reduced to approximately 3/4 of the initial amount). (The amount of urea remaining without being adsorbed is approximately 3/4 of the original amount.) If the amount of urea is reduced to this extent, no problem will occur even if the filtrate is returned to the human blood. According to the present invention, by combining an ultrafiltration method and a fibrous activated carbon adsorbent, urea, uric acid,
It can effectively remove toxic substances such as creatinine, significantly shorten treatment time, and allow long-term use. According to the present invention, the device can be made small and portable, and in addition, it is considerably inexpensive since it does not require the use of dialysate or fluid replacement. The method of the present invention solves the problem of not being able to maintain a mass balance, which was the biggest drawback of conventional filtering artificial kidneys, and from this point alone, the present invention is revolutionary. It can be said to be a thing.
第1図は本発明方法の系統図である。
3:限外濾過器、4:限外濾過膜、7:繊維状
活性炭吸着器、9:脱着用水溶液入口、11:脱
着用水溶液出口。
FIG. 1 is a system diagram of the method of the present invention. 3: ultrafilter, 4: ultrafiltration membrane, 7: fibrous activated carbon adsorber, 9: inlet of aqueous solution for desorption, 11: outlet of aqueous solution for desorption.
Claims (1)
脈からの血液を限外濾過膜で濾過した濾過液中に
含まれる尿素等の有毒物質を除去するに当り、ポ
リアクリロニトリル繊維を原料とした含窒素繊維
状活性炭吸着剤を充填した2個または2個以上の
吸着器を交互または輪番的に用い、1個またはそ
れ以上の吸着器では有毒物質の吸着を行ない、そ
の間に、吸着に利用されていない吸着ずみの吸着
器では有毒物質の脱着を行ない、再生濾過液を静
脈に戻すことを特徴とする人工腎臓装置における
有毒物質の除去方法。1 In removing toxic substances such as urea contained in the filtrate obtained by filtering blood from the artery through an ultrafiltration membrane in an ultrafiltration artificial kidney device, a nitrogen-containing fibrous material made from polyacrylonitrile fiber is used. Two or more adsorbers filled with activated carbon adsorbent are used alternately or in rotation, with one or more adsorbers adsorbing the toxic substance, while the adsorbed material not being used for adsorption is removed. A method for removing toxic substances in an artificial kidney device, characterized by desorbing toxic substances in an adsorption device and returning the regenerated filtrate to the vein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11047278A JPS5538125A (en) | 1978-09-08 | 1978-09-08 | Artificial kidney device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11047278A JPS5538125A (en) | 1978-09-08 | 1978-09-08 | Artificial kidney device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5538125A JPS5538125A (en) | 1980-03-17 |
| JPS649029B2 true JPS649029B2 (en) | 1989-02-16 |
Family
ID=14536564
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11047278A Granted JPS5538125A (en) | 1978-09-08 | 1978-09-08 | Artificial kidney device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5538125A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019107357A1 (en) | 2017-11-29 | 2019-06-06 | 日機装株式会社 | Adsorber regeneration method and dialysis system |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01121062A (en) * | 1987-11-05 | 1989-05-12 | Kanegafuchi Chem Ind Co Ltd | Operational process and device for adsorption system composed of a plurality of adsorbers |
-
1978
- 1978-09-08 JP JP11047278A patent/JPS5538125A/en active Granted
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019107357A1 (en) | 2017-11-29 | 2019-06-06 | 日機装株式会社 | Adsorber regeneration method and dialysis system |
| US11583619B2 (en) | 2017-11-29 | 2023-02-21 | Nikkiso Co., Ltd. | Method for regenerating adsorber and dialysis system |
| US12274820B2 (en) | 2017-11-29 | 2025-04-15 | Nikkiso Co., Ltd. | Method for regenerating adsorber and dialysis system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5538125A (en) | 1980-03-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2086264C1 (en) | Method and device for clearing blood in patients suffering from renal insufficiency | |
| US4581141A (en) | Dialysis material and method for removing uremic substances | |
| US5858238A (en) | Salvage of autologous blood via selective membrane/sorption technologies | |
| US4118314A (en) | Apparatus for treatment of artificial kidney dialyzing fluid | |
| JP2004525747A (en) | Cartridge useful for washing dialysate | |
| JPS645908B2 (en) | ||
| JP7306606B2 (en) | Methods and compositions for removing uremic toxins | |
| CN203507201U (en) | Separating type hemodialysis absorber | |
| JP2002102335A (en) | Blood dialyzer | |
| JPS5825465B2 (en) | Adsorption water removal type blood purification device | |
| JPS649029B2 (en) | ||
| RU93276U1 (en) | EXTRACORPORAL BLOOD CLEANING DEVICE | |
| JP4201313B2 (en) | Toxic substance binding albumin removal system | |
| JP4183036B2 (en) | Blood purification apparatus and regeneration method thereof | |
| GB2083761A (en) | A combination sorbent, dialyser | |
| CN209475256U (en) | A high-efficiency purification and regeneration system for dialysate | |
| SU1012918A1 (en) | Method of cleaning dialyzing solution in artificial kidney apparatus | |
| CN203507204U (en) | Integrated hemodialysis absorber | |
| RU1802713C (en) | Method for organism detoxication | |
| CN108785773B (en) | A high-efficiency purification and regeneration system for dialysate | |
| RU2269363C1 (en) | Method for treating hepatic failure | |
| JPS62236553A (en) | Pretreatment of membrane type blood purifier | |
| JPH08141076A (en) | Blood purifying device and blood purifying means and blood purifying method using this device | |
| Yoshida et al. | Treatment of artificial kidney dialysate with cycling adsorber-desorbers | |
| Van Wagenen et al. | Activated Carbon and The Artificial Kidney I |