JPS6244964B2 - - Google Patents
Info
- Publication number
- JPS6244964B2 JPS6244964B2 JP59121984A JP12198484A JPS6244964B2 JP S6244964 B2 JPS6244964 B2 JP S6244964B2 JP 59121984 A JP59121984 A JP 59121984A JP 12198484 A JP12198484 A JP 12198484A JP S6244964 B2 JPS6244964 B2 JP S6244964B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- gas
- raw material
- raw
- solution
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/04—Feed or outlet devices; Feed or outlet control devices using osmotic pressure using membranes, porous plates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
産業上の利用分野
本発明は、例えば半導体の製造に利用され得る
高純度の薬品、試薬等の溶液を製造するのに用い
られる水溶性ガスの高純度溶液の製造装置に関す
るものである。
従来の技術
例えば半導体製造技術において利用されるよう
な高純度のアンモニア水を製造する場合、従来で
は超純水にアンモニアガスを吹き込む方法が用い
られてきた。しかしこのような方法では、ガス中
の不純物や微粒子等が溶液中に混入するという問
題があり、また超純水に原料ガスを吹き込む方法
では濃度調節を容易にかつ正確に行なうことは困
難であつた。
発明が解決しようとする問題点
そこで、本発明では超純水に原料ガスを吹き込
む代りに原水に疎水性多孔質膜を介して原料ガス
を溶解させることによつてガス中の不純物や微粒
子等の混入の問題および製造すべき溶液濃度の容
易かつ正確な調節の問題を解決することを目的と
している。
問題点を解決するための手段
上述の目的を達成するために、本発明による装
置は、所要の溶液を作るための原水の入口と溶液
の出口とを備えた容器内に疎水性多孔質膜を設
け、この疎水性多孔質膜を介して原料の水溶性ガ
スを原水中に溶解させるに際し、原水の圧力を、
原料として供給される水溶性ガスの圧力に等しい
かそれより高くしかも原水が疎水性多孔質膜を介
して原料として供給される水溶性ガス側に洩れ出
さないまでの値に設定したことを特徴としてい
る。
原料ガスとしては水に溶解するガスであればよ
く、例として、塩化水素、フツ化水素等の無機
質、ギ酸、酢酸等の有機酸、アルコール等の有機
溶媒、塩素ガスおよびアミン類等を挙げることが
できる。
作 用
このように構成した本発明の装置においては、
疎水性多孔質膜を介して原水に原料ガスが溶解さ
れ、従つて原料ガス中に不純物ガスや微粒子等が
あつても原水中に混入することがない。また原料
ガスの供給流量を調整することによつて溶液濃度
を任意に容易に変えることができる。
実施例
以下添附図面を参照して本発明の一実施例につ
いて説明する。
図面には本発明の一実施例による装置の構成を
概略的に示し、1は原水(例えば超純水)の入口
1aと生成された溶液の出口1bとを備えた容器
であり、この容器1内にその長手方向に沿つてほ
ぼ中心軸線上に中空の疎水性多孔質膜2が配置さ
れ、その一端に原料ガス入口部3がまた他端に不
純物出口部4がそれぞれ取付けられている。原料
ガス入口部3は適当な流量調節手段(図示してな
い)を介して図示してない原料ガス供給源に連結
される。中空の疎水性多孔質膜2としては好まし
くは例えばホローフアイバ型の膜部材(例えば、
三菱レーヨン社からポリオレフイン製のホローフ
アイバ膜等が市販されており、外径0.1〜0.5mm程
度、肉厚0.01〜0.2mm程度の中空繊維である)が
用いられる。
このように構成した装置の動作において、超純
水とアンモニアガスを用いて高純度のアンモニア
水を作る場合について説明すると、アンモニアガ
スはガスボンベより適当な圧力を減圧し、そして
流量調整弁等で流量調整された状態で入口部3を
通つて疎水性多孔質膜2内へ供給される。一方容
器1の入口1aから供給される超純水の圧力はア
ンモニアガスの圧力に等しいか或いはそれより高
くされているので供給されたアンモニアガスは実
質的に膜2内の通路を通つて出口部4に向つて流
れる。その際膜2を浸透して内部に入つてくる超
純水中にアンモニアガスが溶解する。なお、原水
の圧力に比べて、原料として供給される水溶性ガ
スの圧力が高くなると、水溶性ガスは原水中に溶
け込まずに泡となつて原水中に入つてしまう。一
方、原水の圧力の上限は上述のように原水が疎水
性多孔質膜を介して原料として供給される水溶性
ガス側に洩れ出さないまでであり、具体的には5
〜10Kg/cm2程度である。この場合アンモニアガス
の流量および透過性の膜2の面積を適当に選択す
ることによつてアンモニアはほとんど全て水に溶
解し、不純物出口部4より出てくるのは極く僅か
である。
下表にアンモニアガスおよび超純水流量とアン
モニア水濃度との例を示す。
INDUSTRIAL APPLICATION FIELD The present invention relates to an apparatus for producing a high-purity solution of a water-soluble gas, which is used to produce a solution of high-purity chemicals, reagents, etc. that can be used, for example, in the production of semiconductors. BACKGROUND ART Conventionally, when producing high-purity ammonia water used in semiconductor manufacturing technology, for example, a method of blowing ammonia gas into ultrapure water has been used. However, with this method, there is a problem that impurities and particulates in the gas get mixed into the solution, and with the method of blowing the raw material gas into ultrapure water, it is difficult to easily and accurately adjust the concentration. Ta. Problems to be Solved by the Invention Therefore, in the present invention, instead of blowing the raw material gas into ultrapure water, the raw water is dissolved in the raw water through a hydrophobic porous membrane, thereby eliminating impurities and fine particles in the gas. The aim is to solve the problem of contamination and easy and accurate adjustment of the concentration of the solution to be produced. Means for Solving the Problems In order to achieve the above-mentioned object, the device according to the invention comprises a hydrophobic porous membrane in a container with an inlet for raw water for making the required solution and an outlet for the solution. When dissolving the raw water-soluble gas in the raw water through this hydrophobic porous membrane, the pressure of the raw water is
The pressure is set to be equal to or higher than the pressure of the water-soluble gas supplied as a raw material, and at a value that does not allow raw water to leak through the hydrophobic porous membrane to the water-soluble gas supplied as a raw material. There is. The raw material gas may be any gas that dissolves in water; examples include inorganic substances such as hydrogen chloride and hydrogen fluoride, organic acids such as formic acid and acetic acid, organic solvents such as alcohol, chlorine gas, and amines. Can be done. Function In the device of the present invention configured as described above,
The raw material gas is dissolved in the raw water through the hydrophobic porous membrane, so even if there are impurity gases or fine particles in the raw water, they will not be mixed into the raw water. Further, the solution concentration can be easily changed arbitrarily by adjusting the supply flow rate of the raw material gas. Embodiment An embodiment of the present invention will be described below with reference to the accompanying drawings. The drawing schematically shows the configuration of an apparatus according to an embodiment of the present invention, in which 1 is a container equipped with an inlet 1a for raw water (for example, ultrapure water) and an outlet 1b for the produced solution; A hollow hydrophobic porous membrane 2 is disposed approximately on the central axis along its longitudinal direction, and a raw material gas inlet 3 and an impurity outlet 4 are attached to one end and the other end, respectively. The raw material gas inlet 3 is connected to a raw material gas supply source (not shown) via a suitable flow rate regulating means (not shown). The hollow hydrophobic porous membrane 2 is preferably, for example, a hollow fiber membrane member (for example,
Hollow fiber membranes made of polyolefin are commercially available from Mitsubishi Rayon Co., Ltd. (hollow fibers with an outer diameter of about 0.1 to 0.5 mm and a wall thickness of about 0.01 to 0.2 mm) are used. In the operation of the device configured in this way, to explain the case of producing high-purity ammonia water using ultrapure water and ammonia gas, the ammonia gas is reduced to an appropriate pressure from a gas cylinder, and then the flow rate is adjusted using a flow rate adjustment valve, etc. It is fed into the hydrophobic porous membrane 2 through the inlet section 3 in a conditioned state. On the other hand, since the pressure of the ultrapure water supplied from the inlet 1a of the container 1 is equal to or higher than the pressure of the ammonia gas, the supplied ammonia gas substantially passes through the passage in the membrane 2 and reaches the outlet. Flows towards 4. At this time, ammonia gas is dissolved in the ultrapure water that permeates through the membrane 2 and enters inside. Note that when the pressure of the water-soluble gas supplied as a raw material becomes higher than the pressure of the raw water, the water-soluble gas does not dissolve into the raw water but enters the raw water in the form of bubbles. On the other hand, as mentioned above, the upper limit of the pressure of raw water is until the raw water does not leak through the hydrophobic porous membrane to the water-soluble gas side that is supplied as a raw material.
~10Kg/ cm2 . In this case, by appropriately selecting the flow rate of ammonia gas and the area of the permeable membrane 2, almost all of the ammonia is dissolved in water, and only a small amount comes out from the impurity outlet 4. The table below shows examples of ammonia gas and ultrapure water flow rates and ammonia water concentrations.
【表】
なお図示実施例は単に例示のためのものであ
り、超純水の供給される容器およびその中に挿置
される透過性膜の形状および構成については必要
に応じて種々変形または変更することができる。
効 果
以上説明してきたように、本発明によれば、原
水に原料ガスを吹き込まずに疎水性多孔質膜を介
して原料ガスを原水中に溶解させるように構成し
ているので、原料ガス中に不純物や微粒子等が含
まれていてもそれらが溶液中に混入することがな
く、また不純物ガスが含まれていても水に溶解し
ていかないので泡として残ることがなく、従つて
高純度の水溶液を得ることができる。また原料ガ
スの流量を調整することによつて所望の濃度の溶
液を容易に作ることができる。[Table] The illustrated embodiments are merely for illustration purposes, and the shape and configuration of the container to which ultrapure water is supplied and the permeable membrane inserted therein may be modified or changed as necessary. can do. Effects As explained above, according to the present invention, the raw material gas is dissolved in the raw water through the hydrophobic porous membrane without blowing the raw material gas into the raw water. Even if the water contains impurities or fine particles, they will not mix into the solution, and even if impurity gases are contained, they will not dissolve in the water and will not remain as bubbles. Aqueous solutions can be obtained. Further, by adjusting the flow rate of the raw material gas, a solution with a desired concentration can be easily prepared.
図面は本発明の一実施例を示す部分断面図であ
る。
図中、1:容器、1a:原水の入口、1b:溶
液の出口、2:疎水性多孔質膜。
The drawing is a partial sectional view showing an embodiment of the present invention. In the figure, 1: container, 1a: raw water inlet, 1b: solution outlet, 2: hydrophobic porous membrane.
Claims (1)
出口とを備えた容器内に疎水性多孔質膜を設け、
この疎水性多孔質膜を介して原料の水溶性ガスを
原水中に溶解させるに際し、原水の圧力を、原料
として供給される水溶性ガスの圧力に等しいかそ
れより高くしかも原水が疎水性多孔質膜を介して
原料として供給される水溶性ガス側に洩れ出さな
いまでの値に設定したことを特徴とする水溶性ガ
スの高純度溶液の製造装置。1. A hydrophobic porous membrane is provided in a container equipped with an inlet for raw water and an outlet for the solution to produce the required solution,
When dissolving a water-soluble gas as a raw material into raw water through this hydrophobic porous membrane, the pressure of the raw water is equal to or higher than the pressure of the water-soluble gas supplied as a raw material, and the raw water is hydrophobic and porous. 1. An apparatus for producing a high-purity solution of a water-soluble gas, characterized in that the value is set to a value that does not leak to the water-soluble gas side supplied as a raw material through a membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59121984A JPS614528A (en) | 1984-06-15 | 1984-06-15 | Manufacturing apparatus of high-purity solution of water-soluble gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59121984A JPS614528A (en) | 1984-06-15 | 1984-06-15 | Manufacturing apparatus of high-purity solution of water-soluble gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS614528A JPS614528A (en) | 1986-01-10 |
| JPS6244964B2 true JPS6244964B2 (en) | 1987-09-24 |
Family
ID=14824684
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59121984A Granted JPS614528A (en) | 1984-06-15 | 1984-06-15 | Manufacturing apparatus of high-purity solution of water-soluble gas |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS614528A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63302926A (en) * | 1987-05-30 | 1988-12-09 | Eruma:Kk | Device for replacing dissolved gas in liquid |
| JPH03293092A (en) * | 1990-04-10 | 1991-12-24 | Ebara Res Co Ltd | Method for removing dissolved oxygen in water |
| EP0893183A3 (en) * | 1993-03-02 | 1999-02-24 | SRI International | Exothermic process with porous means to control reacton rate and exothermic heat |
| US5399188A (en) * | 1993-12-01 | 1995-03-21 | Gas Research Institute | Organic emissions elimination apparatus and process for same |
| KR100956013B1 (en) | 2001-04-23 | 2010-05-06 | 샤이어 인터내쇼날 라이센싱 비.브이. | Pharmaceutical composition for treating kidney stone disease comprising rare earth compound |
| JP6185445B2 (en) * | 2014-10-20 | 2017-08-23 | 株式会社ドクターズ・マン | Hydrogen water supply device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS551816A (en) * | 1978-06-15 | 1980-01-09 | Mitsubishi Rayon Co Ltd | Vapor-liquid contactor |
| JPS5933461Y2 (en) * | 1980-11-17 | 1984-09-18 | 三菱レイヨン株式会社 | Device for dissolving carbon dioxide into drinking water |
-
1984
- 1984-06-15 JP JP59121984A patent/JPS614528A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS614528A (en) | 1986-01-10 |
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