JP3654794B2 - Method and apparatus for reusing chemical liquid for surface treatment - Google Patents

Method and apparatus for reusing chemical liquid for surface treatment Download PDF

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Publication number
JP3654794B2
JP3654794B2 JP19497499A JP19497499A JP3654794B2 JP 3654794 B2 JP3654794 B2 JP 3654794B2 JP 19497499 A JP19497499 A JP 19497499A JP 19497499 A JP19497499 A JP 19497499A JP 3654794 B2 JP3654794 B2 JP 3654794B2
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Japan
Prior art keywords
chamber
exchange resin
treatment
solution
regenerated
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JP19497499A
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JP2001017839A (en
Inventor
明 福永
晴子 大野
利幸 加藤
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Ebara Corp
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Ebara Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Description

【0001】
【発明の属する技術分野】
本発明は、基板の表面処理ないし洗浄にイオン交換樹脂を含む超純水を処理液として使用するに際して、使用済の処理液を電気透析法により脱塩再生し、循環再利用する表面処理用薬液の再利用方法及び装置に関するものである。
【0002】
【従来の技術】
本件発明者らは先に、特願平11−52868号において、被処理材の被処理面をイオン交換体の存在下で超純水と接触させ、該被処理面から溶出するイオン状物質をイオン交換体で除去する表面処理方法を提案している。この方法は、化学薬品を使用しないので、表面に対して薬品によるダメージや汚染を与えることがなく、しかも溶出したイオンはイオン交換体に吸着されるので使用した超純水はほぼそのまま再利用できる。
【0003】
本発明は上記出願に使用した処理液の再利用方法に関するものである。イオン交換体の再生方法としては、陽イオン交換体については、塩酸などの酸と、陰イオン交換体については水酸化ナトリウムなどのアルカリと接触させて、陽イオンについては水素イオンと、陰イオンについては水酸イオンと交換して再生し、余剰の酸・アルカリを水洗することが行われていた。
【0004】
【発明が解決しようとする課題】
イオン交換体が、粒状の樹脂であれば、充てん塔方式などを採用することで上記の方法により容易に再生できるが、表面処理効率ないし洗浄効率を考えて粉末樹脂を使用する場合には、粒径が細かいのでスラリー状でしか扱えず、再生剤や水洗水との分離がきわめて難しいという問題がある。
また、粒状樹脂であっても、再生後の水洗はもっぱら酸ないしアルカリの拡散による希釈で行われるので、水量が多く必要となる。
【0005】
本発明は、上述の事情に鑑みなされたもので、上記従来技術における再生剤や水洗水との分離の困難性の問題や再生後の水洗に多量の水を必要とするという問題を解決することができる表面処理用薬液の再利用方法及び装置を提供することを目的とする。
【0006】
【課題を解決するための手段】
本発明は、使用後の処理液をそのまま電気透析装置の脱イオン室に供給して再生するか、イオン交換樹脂を超純水から分離後、酸ないしアルカリによって再生し、その後電気透析装置の脱イオン室に供給し余剰イオンを除去するものである。
即ち、本発明の1態様は、基板の表面処理ないし洗浄にイオン交換樹脂を分散した超純水を処理液として使用し、使用後の処理液を電気透析装置の脱イオン室に供給して通電脱塩することにより再生し、再生後の再生液を処理液として循環再利用することを特徴とするものである。
本発明の他の態様は、基板の表面処理ないし洗浄にイオン交換樹脂を分散した超純水を処理液として使用し、使用後の処理液中のイオン交換樹脂を分離し、陽イオン交換樹脂については酸で、陰イオン交換樹脂についてはアルカリで再生した後、電気透析装置の脱イオン室に供給して余剰の酸又はアルカリを通電除去し、再生後の再生液を処理液として循環再利用することを特徴とするものである。電気透析装置の濃縮室に超純水を供給するようにしてもよい。
【0007】
【発明の実施の形態】
以下、本発明に係る表面処理用薬液の再利用方法及び装置の実施形態を図面を参照して説明する。
図1は本発明に係る表面処理用薬液の再利用方法の一実施態様を示す概略フロー図である。図1に示すように、洗浄槽5内には、イオン交換樹脂を分散した超純水からなる処理液が収容されており、処理液中に半導体ウエハ等の基板が浸漬されて洗浄される。そして、洗浄後の使用済液6は、再生装置1の脱塩室1aに供給され通電再生される。再生後の再生液2は再生装置1から取出され、貯槽3に貯留される。貯槽3に貯留された再生液は、供給ポンプ4により洗浄槽5に送られ、基板の洗浄に供される。
【0008】
図2は、再生装置の構成を示す概略断面図である。図2に示すように、再生装置1は、電気透析装置から構成され、中央部に配置された脱イオン室を構成する脱塩室1aと、脱塩室1aの両側に配置されるとともに濃縮室を構成する陰極室1eおよび陽極室1fとを備えている。陰極室1eには陰極11が収容され、陽極室1fには陽極12が収容されている。陰極11と陽極12間には直流電源13が接続されている。そして、脱塩室1aと陰極室1eとは陽イオン交換膜1dにより仕切られ、脱塩室1aと陽極室1fとは陰イオン交換膜1cにより仕切られている。また濃縮室を構成する陰極室1eおよび陽極室1fには超純水14が供給されるようになっている。
【0009】
上述の構成において、使用済液6は再生装置1の脱塩室1aに供給される。使用済液中のイオン交換樹脂2aは、基板の表面処理又は洗浄によってイオンを吸着している。イオン交換樹脂2aに吸着されたイオンは、再生装置の脱塩室1aにおいて通電により再生され、陽イオンは陽イオン交換膜1dを介して陰極側へ移動し、陰イオンは陰イオン交換膜1cを介して陽極側へ移動する。陽イオンおよび陰イオンは、それぞれ陰極室1eおよび陽極室1fに供給された超純水14によって再生装置1から廃水8として排出される。脱塩室1aにおいて再生された再生液2は脱塩室1aから排出され、貯槽3に貯留される。
【0010】
図3は本発明の他の実施態様を示す概略フロー図である。図4は樹脂分離槽兼再生槽7と再生装置1の関係を図示した概略図である。
本実施態様は、洗浄槽5と再生装置1との間に分離槽兼再生槽7が配置されている点が図1に示す実施態様と異なっている。その他の構成は図1に示す装置と同様である。
【0011】
図3および図4に示すように、洗浄後の使用済液は、分離槽兼再生槽7に投入され、超純水とイオン交換樹脂に分離される。超純水は再生廃液16として再利用しても良いし、工場の水処理ラインに戻しても良い。分離後のイオン交換樹脂は分離槽兼再生槽7において再生剤17により再生される。この場合、分離後のイオン交換樹脂が陽イオン交換樹脂の場合には、再生剤として酸を用いて再生し、分離後のイオン交換樹脂が陰イオン交換樹脂の場合には、再生剤としてアルカリを用いて再生する。再生後、イオン交換樹脂は再生装置1の脱塩室1aに供給され、完全に再生される。再生装置1におけるイオン交換樹脂2aの再生は前述と同様に行われるが、再生剤として用いた余剰の酸又はアルカリは再生装置1において通電により除去される。
なお分離槽兼再生槽は、1槽であってもよいし、分離槽と再生槽とが分離された2槽であってもよい。
【0012】
【発明の効果】
以上説明したように、本発明は、使用後の処理液をそのまま電気透析装置の脱イオン室に供給して再生するか、イオン交換樹脂を超純水から分離後、酸ないしアルカリによって再生し、その後電気透析装置の脱イオン室に供給し余剰イオンを除去するものである。したがって、従来技術における再生剤や水洗水との分離の困難性の問題や再生後の水洗に多量の水を必要とする問題を解決することができる。
【図面の簡単な説明】
【図1】本発明に係る表面処理用薬液の再利用方法の一実施態様を示す概略フロー図である。
【図2】図1に示す再生装置の構成を示す概略断面図である。
【図3】本発明の他の実施態様を示す概略フロー図である。
【図4】図3に示す分離槽兼再生槽と再生装置の関係を図示した概略図である。
【符号の説明】
1 再生装置
1a 脱塩室
1c 陰イオン交換膜
1d 陽イオン交換膜
1e 陰極室
1f 陽極室
2 再生液
2a イオン交換樹脂
3 貯槽
4 供給ポンプ
5 洗浄槽
6 使用済液
7 分離槽兼再生槽
8 廃水
11 陰極
12 陽極
13 直流電源
14 超純水
16 再生廃液
17 再生剤
[0001]
BACKGROUND OF THE INVENTION
The present invention provides a chemical solution for surface treatment in which, when using ultrapure water containing an ion exchange resin as a treatment liquid for surface treatment or cleaning of a substrate, the used treatment liquid is desalted and regenerated by electrodialysis and reused. The present invention relates to a reusing method and apparatus.
[0002]
[Prior art]
The inventors of the present invention firstly in Japanese Patent Application No. 11-52868, a treated surface of a material to be treated is brought into contact with ultrapure water in the presence of an ion exchanger, and an ionic substance eluted from the treated surface is obtained. A surface treatment method for removing with an ion exchanger has been proposed. Since this method does not use chemicals, there is no chemical damage or contamination on the surface, and the eluted ions are adsorbed to the ion exchanger, so the ultrapure water used can be reused almost as it is. .
[0003]
The present invention relates to a method for reusing a processing solution used in the above application. As a method for regenerating the ion exchanger, the cation exchanger is brought into contact with an acid such as hydrochloric acid, the anion exchanger is brought into contact with an alkali such as sodium hydroxide, the cation is subjected to hydrogen ions and the anions. Was regenerated by exchanging with hydroxide ions, and the excess acid / alkali was washed with water.
[0004]
[Problems to be solved by the invention]
If the ion exchanger is a granular resin, it can be easily regenerated by the above method by adopting a packed tower system or the like, but when using a powder resin in consideration of surface treatment efficiency or cleaning efficiency, Since the diameter is small, it can be handled only in the form of a slurry, and there is a problem that it is extremely difficult to separate from the regenerant and the washing water.
Moreover, even if it is a granular resin, the water washing after reproduction | regeneration is performed by dilution by the spreading | diffusion of an acid thru | or alkali, and requires a lot of water.
[0005]
The present invention has been made in view of the above-described circumstances, and solves the problem of difficulty in separation from the regenerant and the washing water in the above-described prior art and the problem that a large amount of water is required for washing after regeneration. It is an object of the present invention to provide a method and an apparatus for reusing a chemical solution for surface treatment.
[0006]
[Means for Solving the Problems]
In the present invention, the used treatment solution is supplied to the deionization chamber of the electrodialyzer as it is for regeneration, or the ion exchange resin is separated from ultrapure water and then regenerated with acid or alkali, and then the electrodialyzer is removed. It is supplied to the ion chamber to remove excess ions.
That is, according to one aspect of the present invention, ultrapure water in which an ion exchange resin is dispersed is used as a treatment liquid for surface treatment or cleaning of a substrate, and the treatment liquid after use is supplied to a deionization chamber of an electrodialyzer. Regeneration is performed by desalting, and the regenerated solution after regeneration is recycled as a processing solution.
In another aspect of the present invention, ultrapure water in which an ion exchange resin is dispersed is used as a treatment liquid for surface treatment or cleaning of a substrate, and the ion exchange resin in the treatment liquid after use is separated. Is an acid, and the anion exchange resin is regenerated with alkali, then supplied to the deionization chamber of the electrodialyzer to remove excess acid or alkali by energization, and the regenerated regenerated solution is recycled and used as a processing solution. It is characterized by this. You may make it supply ultrapure water to the concentration chamber of an electrodialyzer.
[0007]
DETAILED DESCRIPTION OF THE INVENTION
Embodiments of a method and apparatus for reusing a chemical for surface treatment according to the present invention will be described below with reference to the drawings.
FIG. 1 is a schematic flow diagram showing one embodiment of a method for reusing a chemical solution for surface treatment according to the present invention. As shown in FIG. 1, a processing liquid made of ultrapure water in which an ion exchange resin is dispersed is accommodated in the cleaning tank 5, and a substrate such as a semiconductor wafer is immersed in the processing liquid and cleaned. And the used liquid 6 after washing | cleaning is supplied to the desalination chamber 1a of the reproduction | regeneration apparatus 1, and is electrically regenerated. The regenerated liquid 2 after regeneration is taken out from the regenerator 1 and stored in the storage tank 3. The regenerated liquid stored in the storage tank 3 is sent to the cleaning tank 5 by the supply pump 4 and used for cleaning the substrate.
[0008]
FIG. 2 is a schematic cross-sectional view showing the configuration of the playback apparatus. As shown in FIG. 2, the regenerator 1 is composed of an electrodialyzer, and a demineralization chamber 1a that constitutes a deionization chamber disposed in the center, and a concentration chamber that is disposed on both sides of the demineralization chamber 1a. A cathode chamber 1e and an anode chamber 1f. A cathode 11 is accommodated in the cathode chamber 1e, and an anode 12 is accommodated in the anode chamber 1f. A DC power supply 13 is connected between the cathode 11 and the anode 12. The desalting chamber 1a and the cathode chamber 1e are partitioned by a cation exchange membrane 1d, and the desalting chamber 1a and the anode chamber 1f are partitioned by an anion exchange membrane 1c. Further, ultrapure water 14 is supplied to the cathode chamber 1e and the anode chamber 1f constituting the concentration chamber.
[0009]
In the above-described configuration, the used liquid 6 is supplied to the desalting chamber 1a of the regenerator 1. The ion exchange resin 2a in the used liquid adsorbs ions by surface treatment or cleaning of the substrate. The ions adsorbed on the ion exchange resin 2a are regenerated by energization in the desalination chamber 1a of the regenerator, the cation moves to the cathode side through the cation exchange membrane 1d, and the anion passes through the anion exchange membrane 1c. To the anode side. Cations and anions are discharged from the regenerator 1 as waste water 8 by the ultrapure water 14 supplied to the cathode chamber 1e and the anode chamber 1f, respectively. The regenerated liquid 2 regenerated in the desalting chamber 1 a is discharged from the desalting chamber 1 a and stored in the storage tank 3.
[0010]
FIG. 3 is a schematic flow diagram showing another embodiment of the present invention. FIG. 4 is a schematic view illustrating the relationship between the resin separation tank / regeneration tank 7 and the regenerator 1.
This embodiment is different from the embodiment shown in FIG. 1 in that a separation tank / regeneration tank 7 is disposed between the cleaning tank 5 and the regenerator 1. Other configurations are the same as those of the apparatus shown in FIG.
[0011]
As shown in FIGS. 3 and 4, the used liquid after washing is put into a separation tank / regeneration tank 7 and separated into ultrapure water and an ion exchange resin. The ultrapure water may be reused as the recycled waste liquid 16 or may be returned to the factory water treatment line. The ion exchange resin after separation is regenerated by the regenerant 17 in the separation tank / regeneration tank 7. In this case, when the ion exchange resin after separation is a cation exchange resin, it is regenerated using an acid as a regenerant, and when the ion exchange resin after separation is an anion exchange resin, an alkali is used as a regenerant. Use to play. After regeneration, the ion exchange resin is supplied to the desalting chamber 1a of the regeneration device 1 and completely regenerated. Regeneration of the ion exchange resin 2a in the regenerator 1 is performed in the same manner as described above, but excess acid or alkali used as a regenerant is removed in the regenerator 1 by energization.
The separation tank / regeneration tank may be one tank or two tanks in which the separation tank and the regeneration tank are separated.
[0012]
【The invention's effect】
As described above, the present invention regenerates the used treatment liquid as it is by supplying it to the deionization chamber of the electrodialyzer, or after separating the ion exchange resin from ultrapure water and regenerating it with acid or alkali, Thereafter, it is supplied to the deionization chamber of the electrodialysis apparatus to remove excess ions. Therefore, it is possible to solve the problems of difficulty in separation from the regenerant and washing water in the prior art and the problem of requiring a large amount of water for washing after regeneration.
[Brief description of the drawings]
FIG. 1 is a schematic flow diagram showing one embodiment of a method for reusing a chemical solution for surface treatment according to the present invention.
FIG. 2 is a schematic cross-sectional view showing the configuration of the playback apparatus shown in FIG.
FIG. 3 is a schematic flow diagram showing another embodiment of the present invention.
4 is a schematic view illustrating the relationship between the separation tank / regeneration tank and the regenerator shown in FIG. 3;
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Regenerator 1a Desalination chamber 1c Anion exchange membrane 1d Cation exchange membrane 1e Cathode chamber 1f Anode chamber 2 Regeneration liquid 2a Ion exchange resin 3 Storage tank 4 Supply pump 5 Washing tank 6 Used liquid 7 Separation tank and regeneration tank 8 Waste water 11 Cathode 12 Anode 13 DC power supply 14 Ultrapure water 16 Recycled waste liquid 17 Regenerant

Claims (5)

基板の表面処理ないし洗浄にイオン交換樹脂を分散した超純水を処理液として使用し、使用後の処理液を電気透析装置の脱イオン室に供給して通電脱塩することにより再生し、再生後の再生液を処理液として循環再利用することを特徴とする表面処理用薬液の再利用方法。Uses ultra-pure water with ion-exchange resin dispersed in the surface treatment or cleaning of the substrate as the treatment liquid, and supplies the treatment liquid after use to the deionization chamber of the electrodialysis machine for regeneration and regeneration. A method for reusing a chemical solution for surface treatment, characterized in that a later regenerated solution is circulated and reused as a treatment solution. 基板の表面処理ないし洗浄にイオン交換樹脂を分散した超純水を処理液として使用し、使用後の処理液中のイオン交換樹脂を分離し、陽イオン交換樹脂については酸で、陰イオン交換樹脂についてはアルカリで再生した後、電気透析装置の脱イオン室に供給して余剰の酸又はアルカリを通電除去し、再生後の再生液を処理液として循環再利用することを特徴とする表面処理用薬液の再利用方法。Ultrapure water with ion exchange resin dispersed in the surface treatment or cleaning of the substrate is used as the treatment liquid, and the ion exchange resin in the treatment liquid after use is separated. The cation exchange resin is acid, and the anion exchange resin. After regenerating with alkali, it is supplied to the deionization chamber of the electrodialyzer and the excess acid or alkali is removed by energization, and the regenerated solution after regeneration is recycled and used as a treatment solution. How to reuse chemicals. 電気透析装置の濃縮室に超純水を供給することを特徴とする請求項1又は2記載の表面処理用薬液の再利用方法。The method for reusing a chemical solution for surface treatment according to claim 1 or 2, wherein ultrapure water is supplied to the concentration chamber of the electrodialyzer. 陰イオン交換膜および陽イオン交換膜によって脱イオン室と陽極室と陰極室に分離された電気透析装置と、前記陽極室内の陽極と陰極室内の陰極に通電する直流電源とを備え、基板の表面処理ないし洗浄に用いたイオン交換樹脂を分散した超純水からなる処理液を電気透析装置の脱イオン室に供給して通電脱塩することにより再生し、再生後の再生液を処理液として循環再利用することを特徴とする表面処理用薬液の再利用装置。An electrodialyzer separated into a deionization chamber, an anode chamber, and a cathode chamber by an anion exchange membrane and a cation exchange membrane; and a DC power source for energizing the anode in the anode chamber and the cathode in the cathode chamber; A treatment solution consisting of ultrapure water in which the ion exchange resin used for treatment or washing is dispersed is supplied to the deionization chamber of the electrodialyzer and regenerated by energization and desalination, and the regenerated solution after regeneration is circulated as a treatment solution. An apparatus for reusing a chemical solution for surface treatment, characterized by being reused. 陰イオン交換膜および陽イオン交換膜によって脱イオン室と陽極室と陰極室に分離された電気透析装置と、前記陽極室内の陽極と陰極室内の陰極に通電する直流電源と、使用後の処理液中のイオン交換樹脂を分離するとともに再生する分離槽兼再生槽とを備え、該分離槽兼再生槽にて基板の表面処理ないし洗浄に用いたイオン交換樹脂を分散した超純水からなる処理液中のイオン交換樹脂を分離し、陽イオン交換樹脂については酸で、陰イオン交換樹脂についてはアルカリで再生した後、電気透析装置の脱イオン室に供給して余剰の酸又はアルカリを通電除去し、再生後の再生液を処理液として循環再利用することを特徴とする表面処理用薬液の再利用装置。An electrodialyzer separated into a deionization chamber, an anode chamber and a cathode chamber by an anion exchange membrane and a cation exchange membrane, a direct current power source for energizing the anode in the anode chamber and the cathode in the cathode chamber, and a treatment liquid after use A separation tank / regeneration tank for separating and regenerating the ion exchange resin therein, and a treatment liquid comprising ultrapure water in which the ion exchange resin used for surface treatment or cleaning of the substrate is dispersed in the separation tank / regeneration tank The ion exchange resin is separated, and the cation exchange resin is regenerated with acid, and the anion exchange resin is regenerated with alkali, and then supplied to the deionization chamber of the electrodialyzer to remove excess acid or alkali by energization. An apparatus for reusing a chemical solution for surface treatment, characterized by circulating and reusing the regenerated solution as a treatment solution.
JP19497499A 1999-07-08 1999-07-08 Method and apparatus for reusing chemical liquid for surface treatment Expired - Fee Related JP3654794B2 (en)

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