JPH0796273A - Ultrapure water making apparatus - Google Patents

Ultrapure water making apparatus

Info

Publication number
JPH0796273A
JPH0796273A JP24239993A JP24239993A JPH0796273A JP H0796273 A JPH0796273 A JP H0796273A JP 24239993 A JP24239993 A JP 24239993A JP 24239993 A JP24239993 A JP 24239993A JP H0796273 A JPH0796273 A JP H0796273A
Authority
JP
Japan
Prior art keywords
water tank
pure water
ultrapure water
primary pure
nitrogen gas
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
JP24239993A
Other languages
Japanese (ja)
Other versions
JP2920864B2 (en
Inventor
Yoshinori Kajiyama
吉則 梶山
Kenichi Ushigoe
健一 牛越
Koji Kanazawa
浩二 金澤
Taira Yamamoto
平 山本
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.)
Shinko Pantec Co Ltd
Original Assignee
Shinko Pantec 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 Shinko Pantec Co Ltd filed Critical Shinko Pantec Co Ltd
Priority to JP24239993A priority Critical patent/JP2920864B2/en
Publication of JPH0796273A publication Critical patent/JPH0796273A/en
Application granted granted Critical
Publication of JP2920864B2 publication Critical patent/JP2920864B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the occurrence of air bubbles at the time of heating by connecting the supply parts of the respective circulating passages of a primary pure water tank and an ultrapure water tank to the lower parts under the surfaces of water of the respective pure water tanks to prevent the involution of nitrogen gas at the time of circulation. CONSTITUTION:The primary pure water from a degassing device is supplied into a primary pure water tank 2 and the interior of the primary pure water tank 2 is purged with the nitrogen gas from a nitrogen gas purging device 3. The primary pure water in the primary pure water tank is circulated through a discharge part 5, a circulating passage 8, a UV device 4 and a supply part 14. The supply part 14 of the circulating passage 8 is connected to the lateral wall of the lower part under the surface of pure water of the primary pure tank 2 to prevent the involution of the nitrogen gas. An ultrapure water tank 5 is purged with the nitrogen gas from a nitrogen gas purging device 6 in the same way and ultrapure water is circulated through a discharge part 20, circulating passages 9, 10, a UV device 7 and supply parts 18, 19. These supply parts 18, 19 are connected to the lower part under the surface of ultrapure water of the ultrapure water tank.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は超純水の製造装置、さら
に詳しくは、たとえば半導体工場等に設置される超純水
の製造装置であって、窒素ガスパージを必要とする超純
水の製造装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing ultrapure water, and more particularly to an apparatus for producing ultrapure water which is installed in, for example, a semiconductor factory and which requires nitrogen gas purging. Regarding the device.

【0002】[0002]

【従来の技術】一般に、半導体工場においては、超純水
の製造装置が設置されているが、その製造装置に具備さ
れている水槽において、外部からの汚染を防ぐために窒
素ガスパージが行われている。
2. Description of the Related Art Generally, a semiconductor factory is equipped with an apparatus for producing ultrapure water, and a water tank provided in the apparatus is purged with nitrogen gas in order to prevent contamination from the outside. .

【0003】すなわち、従来のこの種の超純水の製造装
置は、図2に示すように、真空脱気,膜脱気等の各種の
脱気装置1aにより得られた1次純水を貯留するための1
次純水槽2aと、該1次純水槽2aに窒素ガスを注入するた
めの窒素ガスパージ装置3aと、殺菌用のUV装置4aと、
1次純水から供給される純水を貯留するための超純水槽
5aと、該超純水槽5aに窒素ガスを注入するための窒素ガ
スパージ装置6aと、超純水槽5a内の純水をリサイクルす
る際に、純化する2次純水装置7aとを具備したものであ
る。
That is, as shown in FIG. 2, a conventional apparatus for producing ultrapure water of this kind stores primary pure water obtained by various deaerators 1a such as vacuum deaeration and membrane deaeration. 1 to do
A secondary pure water tank 2a, a nitrogen gas purging device 3a for injecting nitrogen gas into the primary pure water tank 2a, a UV device 4a for sterilization,
Ultrapure water tank for storing pure water supplied from primary pure water
5a, a nitrogen gas purging device 6a for injecting nitrogen gas into the ultrapure water tank 5a, and a secondary pure water device 7a for purifying pure water in the ultrapure water tank 5a when recycling is there.

【0004】そして、このような超純水の製造装置にお
いては、循環流路8aによって1次純水槽2a内の純水を循
環,リサイクルして純化し、また循環流路9a及び循環流
路10a によって超純水槽5a内の超純水を循環,リサイク
ルして純化するものである。
In such an ultrapure water producing apparatus, the pure water in the primary pure water tank 2a is circulated and recycled by the circulation passage 8a to purify it, and the circulation passage 9a and the circulation passage 10a. The ultrapure water in the ultrapure water tank 5a is circulated and recycled for purification.

【0005】[0005]

【発明が解決しようとする課題】しかし、従来のこのよ
うな超純水の製造装置においては、循環流路8a,9a,10a
によって循環,リサイクルされる純水を、上部から散水
しつつ1次純水槽2a及び超純水槽5aに流入させるため、
その散水により液面が乱れてパージしている窒素ガスが
超純水中に溶解し、その窒素ガスが気泡となり、気泡粒
子に不純物が付着し、これがウエハ洗浄時に悪影響を及
ぼすおそれがあるという問題点があった。
However, in the conventional apparatus for producing ultrapure water as described above, the circulation channels 8a, 9a, 10a
In order to make the pure water circulated and recycled by the above flow into the primary pure water tank 2a and the ultrapure water tank 5a while spraying water from the top,
The water surface is disturbed by the water spray, and the purged nitrogen gas is dissolved in the ultrapure water, and the nitrogen gas becomes bubbles, and impurities adhere to the bubble particles, which may adversely affect the wafer cleaning. There was a point.

【0006】特に、超純水を加熱した場合には、温度上
昇に伴って気泡の発生も顕著となり、従って上記のよう
な問題点は一層顕著となっていた。
[0006] In particular, when ultrapure water is heated, the generation of bubbles becomes remarkable as the temperature rises, so that the above-mentioned problems become more remarkable.

【0007】本発明は、このような問題点を解決するた
めになされたもので、上記のような超純水中での気泡の
発生、特に加熱時における気泡の発生を防止することを
課題とするものである。
The present invention has been made in order to solve such a problem, and an object thereof is to prevent the generation of bubbles in the ultrapure water as described above, particularly the bubbles during heating. To do.

【0008】[0008]

【課題を解決するための手段】本発明は、このような課
題を解決せんとするもので、その課題を解決するための
手段は、各種の脱気手段により得られた1次純水を貯留
するための1次純水槽2と、前記1次純水槽2から供給
される純水を超純水として貯留するための超純水槽5
と、該1次純水槽2及び超純水槽5にそれぞれ窒素ガス
を注入するための窒素ガスパージ装置3,6と、前記1
次純水槽2及び超純水槽5の純水や超純水をそれぞれ循
環させるべく、該1次純水槽2及び超純水槽5に供給部
と排出部を介して連結された循環流路とを具備した超純
水の製造装置において、前記1次純水槽2及び超純水槽
5のそれぞれの循環流路の供給部が、該1次純水槽2及
び超純水槽5の液面より下部に連結されてなることにあ
る。
The present invention is intended to solve such a problem, and means for solving the problem is to store primary pure water obtained by various degassing means. Primary pure water tank 2 and an ultrapure water tank 5 for storing pure water supplied from the primary pure water tank 2 as ultrapure water.
And nitrogen gas purging devices 3 and 6 for injecting nitrogen gas into the primary pure water tank 2 and the ultrapure water tank 5, respectively.
In order to circulate the pure water and the ultrapure water in the secondary pure water tank 2 and the ultrapure water tank 5, respectively, a circulation flow path connected to the primary pure water tank 2 and the ultrapure water tank 5 via a supply unit and a discharge unit is provided. In the provided apparatus for producing ultrapure water, the supply parts of the respective circulation channels of the primary pure water tank 2 and the ultrapure water tank 5 are connected below the liquid surface of the primary pure water tank 2 and the ultrapure water tank 5. It is to be done.

【0009】[0009]

【作用】すなわち、上記のように1次純水槽2及び超純
水槽5のそれぞれの循環流路の供給部が、前記1次純水
槽2及び超純水槽5の液面より下部に連結されてなるた
め、循環時に窒素ガスを超純水中に巻き込むことがな
く、ひいてはパージしている窒素ガスが超純水中に溶解
することもないのである。
That is, as described above, the supply parts of the respective circulation channels of the primary pure water tank 2 and the ultrapure water tank 5 are connected below the liquid surface of the primary pure water tank 2 and the ultrapure water tank 5. Therefore, the nitrogen gas is not entrained in the ultrapure water during circulation, and the nitrogen gas being purged is not dissolved in the ultrapure water.

【0010】[0010]

【実施例】以下、本発明の実施例について説明する。図
1において、1は真空脱気,膜脱気等の各種の脱気を行
う脱気装置、2は該脱気装置1により得られた1次純水
を貯留するための1次純水槽2で、その1次純水槽2に
はレベルゲージ部11及び純水サンプリング部12が接続さ
れ、レベルゲージ部11と純水サンプリング部12間にはバ
ルブ13が配設されている。
EXAMPLES Examples of the present invention will be described below. In FIG. 1, 1 is a degassing device for performing various degassing processes such as vacuum degassing and membrane degassing, and 2 is a primary pure water tank 2 for storing the primary pure water obtained by the degassing device 1. A level gauge unit 11 and a pure water sampling unit 12 are connected to the primary pure water tank 2, and a valve 13 is arranged between the level gauge unit 11 and the pure water sampling unit 12.

【0011】3は、前記1次純水槽2へ窒素ガスをパー
ジするための窒素ガスパージ装置で、該1次純水槽2の
上部に設けられている。
Reference numeral 3 denotes a nitrogen gas purging device for purging the primary pure water tank 2 with nitrogen gas, which is provided above the primary pure water tank 2.

【0012】8は、前記1次純水槽2内の純水を循環,
リサイクルすべく、供給部14及び排出部15を介して前記
1次純水槽2に連結された循環流路で、その供給部14が
前記1次純水槽2の液面より下部に側方から連結される
ように配設されている。
Numeral 8 circulates the pure water in the primary pure water tank 2.
A circulation channel connected to the primary pure water tank 2 via a supply unit 14 and a discharge unit 15 for recycling, and the supply unit 14 is laterally connected to a portion below the liquid surface of the primary pure water tank 2. It is arranged as described above.

【0013】4は、殺菌用の紫外線装置で、前記循環流
路8の中途部に設けられている。
Reference numeral 4 denotes an ultraviolet device for sterilization, which is provided in the middle of the circulation passage 8.

【0014】5は、前記1次純水槽2から供給される純
水を超純水として貯留するための超純水槽で、流路16を
介して前記循環流路8の中途部に接続されている。
Numeral 5 is an ultrapure water tank for storing the pure water supplied from the primary pure water tank 2 as ultrapure water, which is connected to a midway portion of the circulation flow path 8 via a flow path 16. There is.

【0015】6は、前記超純水槽5へ窒素ガスをパージ
するための窒素ガスパージ装置で、該超純水槽2の上部
に設けられている。
Reference numeral 6 denotes a nitrogen gas purging device for purging the ultrapure water tank 5 with nitrogen gas, which is provided above the ultrapure water tank 2.

【0016】9,10は、前記超純水槽5内の超純水を循
環,リサイクルすべく、供給部18,19 及び排出部20を介
して前記1次純水槽2に連結された循環流路で、排出部
20は前記両流路9,10で共有されている。
Circulation flow paths 9 and 10 are connected to the primary pure water tank 2 through the supply units 18 and 19 and the discharge unit 20 in order to circulate and recycle the ultrapure water in the ultrapure water tank 5. In the discharge section
20 is shared by both channels 9 and 10.

【0017】7は、前記超純水槽5内の純水を循環,リ
サイクルする際に、その純水を純化する2次純水装置
で、前記流路10の中途部に設けられている。そして、こ
の2次純水装置7は、たとえば紫外線照射装置,イオン
交換装置,限外濾過膜等によって構成されている。
Reference numeral 7 is a secondary pure water device for purifying pure water in the ultrapure water tank 5 when circulating and recycling the pure water, which is provided in the middle of the flow path 10. The secondary pure water device 7 is composed of, for example, an ultraviolet irradiation device, an ion exchange device, an ultrafiltration membrane and the like.

【0018】21は、超純水サンプリング部で、バルブ22
を介して前記流路10に接続されている。
Reference numeral 21 is an ultrapure water sampling unit, which is a valve 22.
It is connected to the flow path 10 via.

【0019】そして、上記のような構成からなる超純水
製造装置で超純水を製造する場合について説明すると、
先ず、真空脱気,膜脱気等の各種の脱気装置1により1
次純水を製造し、その1次純水を1次純水槽2へ供給し
て1次純水槽2内で貯留する。
The case of producing ultrapure water with the ultrapure water producing apparatus having the above structure will be described below.
First, the various degassing devices 1 such as vacuum degassing and membrane degassing 1
Secondary pure water is produced, and the primary pure water is supplied to the primary pure water tank 2 and stored in the primary pure water tank 2.

【0020】次に、窒素ガスパージ装置3によって前記
1次純水槽2内に窒素ガスを送り込んで窒素ガスパージ
を行う。
Next, nitrogen gas is sent into the primary pure water tank 2 by the nitrogen gas purging device 3 to perform nitrogen gas purging.

【0021】尚、1次純水槽2内の1次純水は、排出部
15から排出され、循環流路8を循環して供給部14から1
次純水槽2内に供給される。
The primary pure water in the primary pure water tank 2 is discharged from the discharge part.
It is discharged from 15 and circulates in the circulation flow path 8 to 1 from the supply unit 14.
It is then supplied into the pure water tank 2.

【0022】この場合において、循環流路8の供給部14
が前記1次純水槽2の純水の液面より下部に側方から連
結されるように配設されているため、循環時に窒素ガス
を純水中に巻き込むことがなく、この循環流路8を循環
する純水に、上記窒素ガスパージ装置3から1次純水槽
2内に注入される窒素ガスが溶解することもないのであ
る。
In this case, the supply section 14 of the circulation channel 8
Is disposed so as to be laterally connected to a portion below the pure water surface of the primary pure water tank 2, so that nitrogen gas is not entrained in the pure water during circulation, and the circulation flow path 8 The nitrogen gas injected from the nitrogen gas purging device 3 into the primary pure water tank 2 does not dissolve in the pure water circulating in the above.

【0023】また、前記循環流路8の中途部には殺菌用
の紫外線装置4が設けられているため、その紫外線装置
4によって循環する1次純水が殺菌されることとなる。
Further, since the ultraviolet device 4 for sterilization is provided in the middle of the circulation passage 8, the primary pure water circulated by the ultraviolet device 4 is sterilized.

【0024】上述のようにして窒素ガスパージによって
外部からの汚染が防止され、且つ紫外線照射によって殺
菌されつつ循環流路8で循環,リサイクルされた1次純
水槽2側の1次純水が、純化されて超純水として流路16
を介して超純水槽5へ供給され、その超純水槽5で貯留
されることとなる。
As described above, the primary pure water in the primary pure water tank 2 side, which is prevented from being contaminated from the outside by the nitrogen gas purging and sterilized by ultraviolet irradiation, is circulated and recycled in the circulation passage 8 and purified. Flowed as ultrapure water 16
It is supplied to the ultrapure water tank 5 via the tank and stored in the ultrapure water tank 5.

【0025】次に、超純水が供給され貯留された超純水
槽5へは、窒素ガスパージ装置6によって窒素ガスが送
り込まれ、前記1次純水槽2側と同様に窒素ガスパージ
が行なわれる。
Next, nitrogen gas is fed into the ultrapure water tank 5 to which ultrapure water is supplied and stored by the nitrogen gas purging device 6, and the nitrogen gas purge is performed in the same manner as the primary pure water tank 2 side.

【0026】そして、超純水槽5内の超純水は、排出部
20から排出され、2つの循環流路9,10 を循環し、それ
ぞれの循環流路9,10 の供給部18,19 から超純水槽5内
に供給される。
Then, the ultrapure water in the ultrapure water tank 5 is discharged from the discharge portion.
It is discharged from 20 and circulates through the two circulation channels 9 and 10 and is supplied into the ultrapure water tank 5 from the supply portions 18 and 19 of the respective circulation channels 9 and 10.

【0027】この超純水槽5においても、循環流路9,1
0 の供給部18,19 が超純水槽5の純水の貯留部分に側方
から連結されるように配設されているため、前記1次純
水槽2側と同様に、循環流路9,10 を循環する純水に、
窒素ガスパージ装置6からの窒素ガスが溶解することも
ない。
Also in this ultrapure water tank 5, the circulation flow paths 9, 1
Since the supply units 18, 19 of 0 are arranged so as to be connected to the pure water storage portion of the ultrapure water tank 5 from the side, the circulation flow paths 9, 19 are the same as the primary pure water tank 2 side. In pure water circulating 10
The nitrogen gas from the nitrogen gas purging device 6 will not dissolve.

【0028】また、2つの循環流路9,10 のうち、循環
流路10の中途部には上記のような紫外線照射装置,イオ
ン交換装置,限外濾過膜等によって構成される二次純水
装置7が設けられているため、その二次純水装置7によ
って超純水が一層純化されることとなる。
Further, in the middle of the circulation flow passage 10 of the two circulation flow passages 9 and 10, secondary pure water composed of the above-mentioned ultraviolet irradiation device, ion exchange device, ultrafiltration membrane, etc. Since the device 7 is provided, the ultrapure water is further purified by the secondary pure water device 7.

【0029】上述のようにして窒素ガスパージによって
外部からの汚染が防止され、且つ二次純水装置7によっ
て純化が促進されつつ、循環流路9,10 で循環,リサイ
クルされた超純水槽5側の超純水が、加熱等の処理を経
た後、半導体工場等に供給されるのである。
As described above, while the nitrogen gas purge prevents contamination from the outside and the secondary deionizing device 7 promotes purification, the side of the ultrapure water tank 5 which is circulated and recycled in the circulation channels 9 and 10 is provided. The ultrapure water is supplied to a semiconductor factory or the like after being subjected to treatments such as heating.

【0030】以上のように、本実施例においては、1次
純水槽2及び超純水槽5のいずれの純水槽においても、
純水の循環経路8,9,10の供給部14,18,19が、それぞ
れ1次純水槽2及び超純水槽5の液面より下部に側方か
ら連結されるように配設されているため、両純水槽2,
5の双方ともに窒素ガスの混入が防止されることとな
り、その結果、加熱処理時の気泡の発生が防止されるこ
ととなるのである。
As described above, in this embodiment, in any of the pure water tanks of the primary pure water tank 2 and the ultrapure water tank 5,
The supply parts 14, 18, 19 of the pure water circulation paths 8, 9, 10 are arranged so as to be laterally connected below the liquid surfaces of the primary pure water tank 2 and the ultrapure water tank 5, respectively. Therefore, both deionized water tanks 2,
In both cases, mixture of nitrogen gas is prevented, and as a result, generation of bubbles during heat treatment is prevented.

【0031】尚、上記のような1次純水槽2や超純水槽
5から純水をサンプリングし、図3に示すような加熱装
置を用いて水を加熱し、発生する気泡量を温度を変えて
測定し、それから溶存ガス量を求めた。また、発生した
ガスを回収し、化学分析も行った。
Pure water is sampled from the primary pure water tank 2 and the ultrapure water tank 5 as described above, and the water is heated using a heating device as shown in FIG. Then, the amount of dissolved gas was obtained. In addition, the generated gas was recovered and chemical analysis was performed.

【0032】これをより詳細に説明すると、前記超純水
製造装置における一次純水槽2側の純水サンプリング部
12と、超純水槽5側のサンプリング部21とでサンプリン
グされた純水が、図3のヒータ23で加熱されると、補集
びん24内で気泡を発生し、その気泡がガス分析用サンプ
ル袋25で補集され、その補集されたガスによって溶存ガ
ス量が求められ、また化学分析が行われることとなるの
である。
This will be described in more detail. Pure water sampling unit on the side of the primary pure water tank 2 in the ultrapure water production system.
When pure water sampled by 12 and the sampling unit 21 on the side of the ultrapure water tank 5 is heated by the heater 23 of FIG. 3, bubbles are generated in the collection bottle 24, and the bubbles generate gas analysis sample. The bag 25 collects the dissolved gas, the dissolved gas amount is determined by the collected gas, and the chemical analysis is performed.

【0033】測定温度は、40℃,55℃, 70℃,80℃でそ
れぞれ行った。
The measurement temperatures were 40 ° C., 55 ° C., 70 ° C. and 80 ° C., respectively.

【0034】さらに、従来の超純水製造装置でサンプリ
ングした純水,超純水との加熱発生ガス量を比較した。
Further, the amounts of heat-generated gas of pure water and ultrapure water sampled by a conventional ultrapure water production apparatus were compared.

【0035】その結果のグラフを図4に示す。A graph of the result is shown in FIG.

【0036】図4において、(イ)は純水槽からサンプ
リングした純水を加熱して発生したガス量に関するもの
で、(ロ)は超純水槽からサンプリングした超純水を加
熱して発生したガス量に関するものである。
In FIG. 4, (a) relates to the amount of gas generated by heating the pure water sampled from the pure water tank, and (b) shows the gas generated by heating the ultrapure water sampled from the ultrapure water tank. It is about quantity.

【0037】図4(イ)のグラフにおいて、Aは本実施
例の測定結果、B〜Fは従来の装置を備えた複数の工場
でそれぞれ測定した結果を示す。
In the graph of FIG. 4 (A), A indicates the measurement result of this embodiment, and B to F indicate the results of measurement at a plurality of factories equipped with conventional devices.

【0038】また、図4(ロ)のグラフにおいて、aは
本実施例の測定結果、b〜hは従来の装置を備えた複数
の工場でそれぞれ測定した結果を示す。
Further, in the graph of FIG. 4B, a shows the measurement result of this embodiment, and b to h show the measurement results at a plurality of factories equipped with the conventional apparatus.

【0039】この図4の結果からも明らかなように、従
来の製造装置でサンプリングしたものは、40℃程度の水
温ではほとんど気泡の発生が認められないものの、温度
が高くなるにつれ発生ガス量も増加し、80℃の温度では
かなりのガスの発生が認められた。
As is clear from the results shown in FIG. 4, the sample produced by the conventional manufacturing apparatus shows almost no bubbles at a water temperature of about 40 ° C., but the amount of gas produced increases as the temperature rises. Increased, and considerable gas evolution was observed at a temperature of 80 ° C.

【0040】これに対して、本実施例では、温度が低い
場合はもちろん、80℃に加熱してもガスの発生はほとん
ど認められなかった。
On the other hand, in the present example, almost no gas generation was observed not only when the temperature was low but also when heated to 80 ° C.

【0041】尚、上記実施例では、1次純水槽2側の循
環流路8の途中部に紫外線装置4を設け、超純水槽5側
の循環流路10の途中部に2次純水装置7を設けたため、
1次純水槽2及び超純水槽5でそれぞれ循環,リサイク
ルされる純水や超純水の純度が高まるという好ましい効
果が得られたが、このような紫外線装置4や2次純水装
置7を設けることは本発明に必須の条件ではない。
In the above embodiment, the ultraviolet device 4 is provided in the middle of the circulation flow path 8 on the side of the primary pure water tank 2 and the secondary pure water device is provided in the middle of the circulation flow path 10 on the side of the ultrapure water tank 5. Because 7 is provided,
The desirable effect of increasing the purity of pure water and ultrapure water which are circulated and recycled in the primary pure water tank 2 and the ultrapure water tank 5, respectively, was obtained. The provision is not an essential condition for the present invention.

【0042】また、その他の各構成部分も本発明の意図
する範囲で設計変更自在である。
Further, the design of each of the other constituent parts can be freely changed within the scope intended by the present invention.

【0043】さらに、上記実施例では、循環流路8,
9,10の供給部14,18,19が、1次純水槽2及び超純水槽
5の貯留部分に側方から連結されているが、これに限ら
ず、たとえば1次純水槽2及び超純水槽5の底部に連結
することも可能である。
Further, in the above embodiment, the circulation flow path 8,
The supply parts 14, 18, 19 of 9, 10 are laterally connected to the storage parts of the primary pure water tank 2 and the ultrapure water tank 5, but not limited to this, for example, the primary pure water tank 2 and the ultrapure water tank. It is also possible to connect to the bottom of the water tank 5.

【0044】要は、1次純水槽2及び超純水槽5にそれ
ぞれ窒素ガスを注入するための窒素ガスパージ装置3,
6と、1次純水槽2及び超純水槽5に供給部14,18,19と
排出部15,20 を介して連結された循環流路8,9,10と
が具備され、且つその循環流路8,9,10の供給部14,1
8,19が、上記1次純水槽2及び超純水槽5の液面より下
部に連結されていればよいのである。
In short, a nitrogen gas purging device 3 for injecting nitrogen gas into the primary pure water tank 2 and the ultrapure water tank 5, respectively.
6, the primary pure water tank 2 and the ultrapure water tank 5 are provided with circulation flow paths 8, 9 and 10 connected to the primary pure water tank 2 and the ultrapure water tank 5 through the supply units 14, 18 and 19 and the discharge units 15 and 20, and the circulation flow thereof. Supply section 14,1 of paths 8, 9 and 10
It suffices that 8, 19 are connected below the liquid surfaces of the primary pure water tank 2 and the ultrapure water tank 5.

【0045】[0045]

【発明の効果】叙上のように、本発明は、1次純水槽及
び超純水槽のそれぞれの循環流路の供給部は従来のよう
に1次純水槽及び超純水槽の水面の上部に離間しておら
ず、その1次純水槽及び超純水槽の液面より下部に連結
されているため、パージされる窒素ガスは従来のように
散水される超純水等に溶解するようなこともなく、その
窒素ガスの超純水中への不用意な溶解が防止されること
となる。
As described above, according to the present invention, the supply portions of the respective circulation channels of the primary pure water tank and the ultrapure water tank are located above the water surfaces of the primary pure water tank and the ultrapure water tank as in the conventional case. The nitrogen gas to be purged should not dissolve in the primary pure water tank and the ultrapure water tank below the liquid level, so the nitrogen gas to be purged should be dissolved in the ultrapure water to be sprayed as in the past. Nonetheless, the nitrogen gas is prevented from being inadvertently dissolved in the ultrapure water.

【0046】この結果、加熱処理によって超純水中に気
泡が発生するおそれもなく、従って従来のような気泡粒
子の不純物への付着が防止され、よってウエハ洗浄等に
悪影響を及ぼすおそれがあるという問題点も解決するこ
とが可能となる。
As a result, there is no possibility that air bubbles will be generated in the ultrapure water due to the heat treatment, and therefore, adhesion of air bubble particles to impurities as in the conventional case can be prevented, which may adversely affect wafer cleaning and the like. It also becomes possible to solve problems.

【図面の簡単な説明】[Brief description of drawings]

【図1】一実施例の超純水製造装置の概略ブロック図。FIG. 1 is a schematic block diagram of an ultrapure water production system according to an embodiment.

【図2】従来の超純水製造装置の概略ブロック図。FIG. 2 is a schematic block diagram of a conventional ultrapure water production system.

【図3】一試験例の加熱装置の概略ブロック図。FIG. 3 is a schematic block diagram of a heating device of a test example.

【図4】試験結果を示すグラフで、(イ)は純水を加熱
して発生したガス量、(ロ)は超純水を加熱して発生し
たガス量のグラフ。
FIG. 4 is a graph showing test results, where (a) is a gas amount generated by heating pure water and (b) is a graph of gas amount generated by heating ultrapure water.

【符号の説明】[Explanation of symbols]

2…1次純水槽 3…窒素ガスパージ装
置 5…超純水槽 6…窒素ガスパージ装
2 ... Primary pure water tank 3 ... Nitrogen gas purging device 5 ... Ultra pure water tank 6 ... Nitrogen gas purging device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 各種の脱気手段により得られた1次純水
を貯留するための1次純水槽(2) と、前記1次純水槽
(2) から供給される純水を超純水として貯留するための
超純水槽(5) と、該1次純水槽(2) 及び超純水槽(5) に
それぞれ窒素ガスを注入するための窒素ガスパージ装置
(3),(6) と、前記1次純水槽(2) 及び超純水槽(5) の純
水や超純水をそれぞれ循環させるべく、該1次純水槽
(2) 及び超純水槽(5) に供給部と排出部を介して連結さ
れた循環流路とを具備した超純水の製造装置において、
前記1次純水槽(2) 及び超純水槽(5) のそれぞれの循環
流路の供給部が、該1次純水槽(2) 及び超純水槽(5) の
液面より下部に連結されてなることを特徴とする超純水
の製造装置。
1. A primary pure water tank (2) for storing primary pure water obtained by various degassing means, and the primary pure water tank.
An ultrapure water tank (5) for storing the pure water supplied from (2) as ultrapure water, and a tank for injecting nitrogen gas into the primary pure water tank (2) and the ultrapure water tank (5), respectively. Nitrogen gas purging device
In order to circulate the pure water and ultrapure water in (3) and (6) and the primary pure water tank (2) and the ultrapure water tank (5), respectively.
(2) and an ultrapure water production apparatus comprising a circulation channel connected to the ultrapure water tank (5) through a supply unit and a discharge unit,
The supply parts of the circulation channels of the primary pure water tank (2) and the ultrapure water tank (5) are connected below the liquid surface of the primary pure water tank (2) and the ultrapure water tank (5). An apparatus for producing ultrapure water, which is characterized in that
JP24239993A 1993-09-29 1993-09-29 Ultrapure water production equipment Expired - Fee Related JP2920864B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24239993A JP2920864B2 (en) 1993-09-29 1993-09-29 Ultrapure water production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24239993A JP2920864B2 (en) 1993-09-29 1993-09-29 Ultrapure water production equipment

Publications (2)

Publication Number Publication Date
JPH0796273A true JPH0796273A (en) 1995-04-11
JP2920864B2 JP2920864B2 (en) 1999-07-19

Family

ID=17088570

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24239993A Expired - Fee Related JP2920864B2 (en) 1993-09-29 1993-09-29 Ultrapure water production equipment

Country Status (1)

Country Link
JP (1) JP2920864B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2503107A (en) * 2012-06-13 2013-12-18 Vws Uk Ltd Providing purified water

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2503107A (en) * 2012-06-13 2013-12-18 Vws Uk Ltd Providing purified water
GB2503107B (en) * 2012-06-13 2014-07-02 Vws Uk Ltd Method and system for providing purified water
US10414676B2 (en) 2012-06-13 2019-09-17 Vws (Uk) Ltd. Method and system for providing purified water

Also Published As

Publication number Publication date
JP2920864B2 (en) 1999-07-19

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