JPH04126524A - Diffusion dialysis - Google Patents
Diffusion dialysisInfo
- Publication number
- JPH04126524A JPH04126524A JP24609290A JP24609290A JPH04126524A JP H04126524 A JPH04126524 A JP H04126524A JP 24609290 A JP24609290 A JP 24609290A JP 24609290 A JP24609290 A JP 24609290A JP H04126524 A JPH04126524 A JP H04126524A
- Authority
- JP
- Japan
- Prior art keywords
- agent
- diffusion dialysis
- benzisothiazolin
- antimold
- mold
- 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
- 238000000502 dialysis Methods 0.000 title claims abstract description 13
- 238000009792 diffusion process Methods 0.000 title claims abstract description 12
- 238000011084 recovery Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims abstract description 9
- DMSMPAJRVJJAGA-UHFFFAOYSA-N benzo[d]isothiazol-3-one Chemical compound C1=CC=C2C(=O)NSC2=C1 DMSMPAJRVJJAGA-UHFFFAOYSA-N 0.000 claims abstract description 7
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims abstract description 4
- JYEUMXHLPRZUAT-UHFFFAOYSA-N 1,2,3-triazine Chemical compound C1=CN=NN=C1 JYEUMXHLPRZUAT-UHFFFAOYSA-N 0.000 claims abstract description 3
- SZXQTJUDPRGNJN-UHFFFAOYSA-N dipropylene glycol Chemical compound OCCCOCCCO SZXQTJUDPRGNJN-UHFFFAOYSA-N 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims abstract description 3
- 239000003429 antifungal agent Substances 0.000 claims description 8
- 229940121375 antifungal agent Drugs 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 230000000855 fungicidal effect Effects 0.000 claims 1
- 239000000417 fungicide Substances 0.000 claims 1
- 239000003014 ion exchange membrane Substances 0.000 abstract description 6
- 239000002253 acid Substances 0.000 abstract description 5
- 238000004140 cleaning Methods 0.000 abstract description 5
- 239000007788 liquid Substances 0.000 abstract description 4
- 239000003795 chemical substances by application Substances 0.000 abstract 7
- 229960004063 propylene glycol Drugs 0.000 abstract 1
- 235000013772 propylene glycol Nutrition 0.000 abstract 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 12
- 230000001954 sterilising effect Effects 0.000 description 6
- 238000004659 sterilization and disinfection Methods 0.000 description 5
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 4
- 239000003011 anion exchange membrane Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 230000005856 abnormality Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000000385 dialysis solution Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- -1 sulfuric acid Chemical class 0.000 description 1
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は拡散透析法、特にカビの発生を防止した拡散透
析法に係るものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a diffusion dialysis method, particularly a diffusion dialysis method that prevents the growth of mold.
[従来の技術]
従来より、酸回収用として陰イオン交換膜を使用する拡
散透析法は広く実用化されている。[Prior Art] Diffusion dialysis using an anion exchange membrane has been widely put into practical use for acid recovery.
この場合、特に硫酸を回収しようとする場合、陰イオン
交換膜の表面にカビが発生、繁殖する。これを防止する
為に、被拡散透析液及び/又は回収用水を予め紫外線殺
菌設備により殺菌したり、或は定期的にホルマリン溶液
を張り込む等の対策がとられている。In this case, especially when attempting to recover sulfuric acid, mold grows and grows on the surface of the anion exchange membrane. In order to prevent this, measures are taken such as sterilizing the diffused dialysate and/or recovered water in advance using ultraviolet sterilization equipment, or periodically filling the dialysis fluid with formalin solution.
[発明が解決しようとする課題]
しかしながら、紫外線殺菌は一過性であり、その後に侵
入するカビには何らの効果がなく、又ホルマリン溶液に
よる定期的な殺菌は、効果が比較的弱く、又臭気や排水
等問題が生じ、好ましい方法でない。[Problems to be solved by the invention] However, ultraviolet sterilization is temporary and has no effect on mold that invades afterward, and periodic sterilization with formalin solution has a relatively weak effect, and This is not the preferred method as it causes problems such as odor and drainage.
か(して、カビにより汚染されたイオン交換膜は、解体
洗浄により除去しているのが現状である。この解体洗浄
には多大な労力と時間を要するのみならず、イオン交換
膜に人為的なダメージを与え、ひいてはイオン交換膜の
寿命を短くする致命的な欠点を有している。Currently, ion exchange membranes contaminated with mold are removed by disassembly and cleaning.This disassembly and cleaning not only requires a great deal of labor and time, but also causes artificial damage to the ion exchange membrane. It has the fatal disadvantage of causing serious damage and shortening the life of the ion exchange membrane.
[課題を解決する為の手段]
本発明者は、このような点に鑑み、解体洗浄を行なうこ
とな(、有効にカビの発生を防止することを目的として
種々研究、検討した結果、被拡散透析液及び/又は回収
用水中に1.2−ベンズイソチアゾリン−3−オンを存
在させることにより前記目的を達成し得ることを見出し
、本発明はこれを要旨とするものである。[Means for Solving the Problems] In view of the above, the inventor of the present invention has conducted various research and examinations with the aim of effectively preventing the growth of mold (without disassembling and cleaning it). It has been found that the above object can be achieved by the presence of 1,2-benzisothiazolin-3-one in the dialysate and/or the recovery water, and this is the gist of the present invention.
本発明において、防カビ剤はイオン交換膜への影響、回
収された酸中への残存の問題、防カビ剤自体の人体への
影響等が考慮されねばならない。この為、用いられる防
カビ剤はエチレンジアミン、ジプロピレングリコール、
プロピレングリコール、トリアジンの水溶液若しくは配
合混合物を用いるのが適当である。In the present invention, the influence of the antifungal agent on the ion exchange membrane, the problem of remaining in the recovered acid, the influence of the antifungal agent itself on the human body, etc. must be taken into consideration. For this reason, the antifungal agents used are ethylenediamine, dipropylene glycol,
It is suitable to use aqueous solutions or blended mixtures of propylene glycol, triazine.
本発明に用いられる防カビ剤の使用量は、あまり多すぎ
ても回収液中に残存する量が多く、回収液の純度を損ね
、又あまり少なすぎても効果が不充分となり何れも好ま
しくない。この為、使用量は0.11−1O0pp、好
ましくは1〜10−ppm程度を採用するのが適当であ
る。実際の使用に当たっては、これら防カビ剤を回収用
水中に所定量加えるだけでよいが、拡散透析に際し、供
給される被透析液中にも防カビ剤や紫外線殺菌を行なう
ほうが好ましい。被透析液としては、例えば硫酸の回収
等酸の回収、アルカリの回収等に適宜使用できる。If the amount of the antifungal agent used in the present invention is too large, a large amount will remain in the recovered liquid, impairing the purity of the recovered liquid, and if it is too small, the effect will be insufficient, both of which are undesirable. . For this reason, it is appropriate to adopt an amount of about 0.11-100 ppm, preferably about 1-10 ppm. In actual use, it is sufficient to simply add a predetermined amount of these antifungal agents to the water for recovery, but during diffusion dialysis, it is preferable to also apply an antifungal agent and ultraviolet sterilization to the dialysate fluid supplied. The fluid to be dialysed can be appropriately used for recovering acids such as sulfuric acid, recovering alkalis, and the like.
[実施例]
陰イオン交換膜100枚を組み込んだ旭硝子■製F−O
W型拡散透析槽を2基準備し、硫酸300g/12、硫
酸アルミニウム120g/βの原液からの硫酸回収を常
法に従って実施した。2基の使用回収用水はイオン交換
純水を使用し、予め千代田工販■製紫外線殺菌装置5H
−IDにより殺菌を行なった。[Example] Asahi Glass F-O incorporating 100 anion exchange membranes
Two W-type diffusion dialysis tanks were prepared, and sulfuric acid recovery from a stock solution of 300 g/12 sulfuric acid and 120 g/β aluminum sulfate was performed according to a conventional method. The water for use and recovery in the two units uses ion-exchanged pure water, and is preheated using an ultraviolet sterilizer 5H manufactured by Chiyoda Kohan ■.
- Sterilization was performed by ID.
そして、一方の拡散透析槽の回収用水、及び被透析液中
には更に1.2−ベンズイソチアゾリン−3−オンのエ
チレンジアミン水溶液(有効成分濃度33%)を3 p
pm連続添加した。供給流量は同一条件とし、原液は5
.07β/時、回収用水は5.Oj2/時とした。当初
硫酸回収率は両者とも82%であったが、紫外線だけの
イオン交換水を使用したものは1ケ月後より次第に回収
率が低下し、4ケ月後には68%まで低下した。Further, 3 p of an ethylenediamine aqueous solution of 1,2-benzisothiazolin-3-one (active ingredient concentration 33%) was added to the recovery water of one diffusion dialysis tank and the dialysate.
pm was added continuously. The supply flow rate is the same, and the stock solution is 5.
.. 07β/hour, water for recovery is 5. Oj2/hour. Initially, the sulfuric acid recovery rate was 82% in both cases, but in the case where ion-exchanged water with only ultraviolet rays was used, the recovery rate gradually decreased after one month and dropped to 68% after four months.
これに対し、1.2−ベンズイソチアゾリン−3−オン
を添加しているものは安定した硫酸回収率を維持し、4
ケ月後もその値は82%であった。この時点で解体点検
を行なったところ、紫外線だけの殺菌を行なっているイ
オン交換膜を使用しているものは、回収酸室の上部約%
に糸状のカビが多量に繁殖していた。1.2−ベンズイ
ソチアゾリン−3−オンを添加してものについては、何
ら異常は発見できなかった。On the other hand, the one to which 1,2-benzisothiazolin-3-one was added maintained a stable sulfuric acid recovery rate and
After several months, the value remained at 82%. At this point, a disassembly and inspection was conducted, and it was found that approximately 30% of the upper part of the recovery acid chamber was using an ion-exchange membrane that sterilized only with ultraviolet light.
There was a large amount of filamentous mold growing. No abnormality was found in the sample to which 1,2-benzisothiazolin-3-one was added.
Claims (1)
ズイソチアゾリン−3−オンからなる防カビ剤を存在さ
せることを特徴とする拡散透析法。 2、防カビ剤はエチレンジアミン、ジプロピレングリコ
ール、プロピレングリコール、トリアジンの水溶液若し
くは配合混合物である請求項1の拡散透析法。 3、防カビ剤は0.1〜100ppm存在させる請求項
1の拡散透析法。[Scope of Claims] 1. A diffusion dialysis method characterized in that an antifungal agent consisting of 1,2-benzisothiazolin-3-one is present in the dialysate to be diffused and/or in the water for recovery. 2. The diffusion dialysis method according to claim 1, wherein the fungicide is an aqueous solution or a blended mixture of ethylenediamine, dipropylene glycol, propylene glycol, and triazine. 3. The diffusion dialysis method according to claim 1, wherein the antifungal agent is present in an amount of 0.1 to 100 ppm.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2-201302 | 1990-07-31 | ||
JP20130290 | 1990-07-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04126524A true JPH04126524A (en) | 1992-04-27 |
Family
ID=16438746
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24609290A Pending JPH04126524A (en) | 1990-07-31 | 1990-09-18 | Diffusion dialysis |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04126524A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008272667A (en) * | 2007-04-27 | 2008-11-13 | Japan Organo Co Ltd | Reverse osmosis membrane treatment agent and reverse osmosis membrane treatment method using it |
-
1990
- 1990-09-18 JP JP24609290A patent/JPH04126524A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008272667A (en) * | 2007-04-27 | 2008-11-13 | Japan Organo Co Ltd | Reverse osmosis membrane treatment agent and reverse osmosis membrane treatment method using it |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2599204B2 (en) | Hemodialysis agent | |
JP5685271B2 (en) | Sterile composition containing peracetic acid without molybdate | |
AU593555B2 (en) | Sterilant compositions | |
ATE242013T1 (en) | DEVICE FOR WASHING AND DISINFECTING DIALYZERS USING ELECTROLYTICALLY PRODUCED ACID WATER | |
EP3233138B1 (en) | Cleaning composition | |
JPS6022946B2 (en) | Sterilization method for biological dialysis equipment | |
WO2009006493A3 (en) | 'extended use dialysis system' | |
JPH09503417A (en) | Dialyzer and reprocessing method | |
CA2000586C (en) | Method of cleaning and/or disinfecting and sterilizing hemodyalisis apparatus | |
US5178830A (en) | Method of cleaning, disinfecting and sterilizing hemodialysis apparatus | |
JP3053550B2 (en) | How to clean medical equipment | |
JP2606910B2 (en) | Ultrapure water production and supply equipment | |
JPH04126524A (en) | Diffusion dialysis | |
CN108201628A (en) | Including the method with process cycle in the post processing of acid concentrate combination type sterilizing and decalcification and preparation extracorporeal blood treat-ment apparatus | |
US6419850B1 (en) | System and composition for decontaminating fluids | |
JP4332829B2 (en) | Dialysis system | |
JP2694503B2 (en) | Blood circulation in artificial dialysis, sterilization and purification method for dialysate piping pipeline | |
JPH04135559A (en) | Disinfecting detergent for medical treating equipment for artificial dialysis or the like | |
JPH084787B2 (en) | Liquid processing machine element | |
JPH03229416A (en) | Method of sterilization washing of circulation route of pure water for washing in semiconductor manufacture | |
JPH05329340A (en) | Membrane module | |
KR101279557B1 (en) | Method for reusing dialyzer | |
JP2012187321A (en) | Method for washing and disinfecting dialysate line in artificial dialyzer | |
JP3020709U (en) | Aseptic. Water purifier for odorless water supply | |
JPH0630765B2 (en) | Aseptic pure water supply method |