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JPH0252537B2 - - Google Patents
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JPH0252537B2 - - Google Patents

Info

Publication number
JPH0252537B2
JPH0252537B2 JP6220183A JP6220183A JPH0252537B2 JP H0252537 B2 JPH0252537 B2 JP H0252537B2 JP 6220183 A JP6220183 A JP 6220183A JP 6220183 A JP6220183 A JP 6220183A JP H0252537 B2 JPH0252537 B2 JP H0252537B2
Authority
JP
Japan
Prior art keywords
liquid
zone
container
carrier gas
reactive liquid
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
Application number
JP6220183A
Other languages
Japanese (ja)
Other versions
JPS59189932A (en
Inventor
Yutaka Yoriume
Juichi Noda
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.)
NTT Inc
Original Assignee
Nippon Telegraph and Telephone Corp
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 Nippon Telegraph and Telephone Corp filed Critical Nippon Telegraph and Telephone Corp
Priority to JP6220183A priority Critical patent/JPS59189932A/en
Publication of JPS59189932A publication Critical patent/JPS59189932A/en
Publication of JPH0252537B2 publication Critical patent/JPH0252537B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/001Feed or outlet devices as such, e.g. feeding tubes
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B37/00Manufacture or treatment of flakes, fibres, or filaments from softened glass, minerals, or slags
    • C03B37/01Manufacture of glass fibres or filaments
    • C03B37/012Manufacture of preforms for drawing fibres or filaments
    • C03B37/014Manufacture of preforms for drawing fibres or filaments made entirely or partially by chemical means, e.g. vapour phase deposition of bulk porous glass either by outside vapour deposition [OVD], or by outside vapour phase oxidation [OVPO] or by vapour axial deposition [VAD]
    • C03B37/01413Reactant delivery systems
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/80Feeding the burner or the burner-heated deposition site
    • C03B2207/85Feeding the burner or the burner-heated deposition site with vapour generated from liquid glass precursors, e.g. directly by heating the liquid
    • C03B2207/86Feeding the burner or the burner-heated deposition site with vapour generated from liquid glass precursors, e.g. directly by heating the liquid by bubbling a gas through the liquid
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/80Feeding the burner or the burner-heated deposition site
    • C03B2207/85Feeding the burner or the burner-heated deposition site with vapour generated from liquid glass precursors, e.g. directly by heating the liquid
    • C03B2207/89Controlling the liquid level in or supply to the tank
    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B2207/00Glass deposition burners
    • C03B2207/80Feeding the burner or the burner-heated deposition site
    • C03B2207/90Feeding the burner or the burner-heated deposition site with vapour generated from solid glass precursors, i.e. by sublimation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は半導体結晶のエピタキシヤル成長、半
導体への不純物拡散、アモルフアス薄膜、絶縁膜
の成長、石英系光フアイバーの製造等における原
料である反応性液体を収容するための反応性液体
容器に関する。
[Detailed Description of the Invention] [Field of Application of the Invention] The present invention is directed to the epitaxial growth of semiconductor crystals, the diffusion of impurities into semiconductors, the growth of amorphous thin films, insulating films, the production of silica-based optical fibers, etc. The present invention relates to a reactive liquid container for containing a liquid.

〔従来技術〕[Prior art]

従来、上記のような反応性液体を反応容器内に
輸送して所望の反応をさせるには、反応性液体を
収容する容器内にキヤリアガスを導入し、該液体
の蒸気とともに反応容器へ輸送する方法が行なわ
れていた。このような場合、キヤリアガスを反応
性液体容器へ導入する方法として、キヤリアガス
の導入口を反応性液体容器内の反応性液体の液面
上に設ける方法と、液面下に設ける方法がある。
Conventionally, in order to transport the above-mentioned reactive liquid into a reaction container and cause the desired reaction, a carrier gas is introduced into a container containing the reactive liquid, and the liquid is transported together with the vapor of the liquid to the reaction container. was being carried out. In such a case, there are two methods for introducing the carrier gas into the reactive liquid container: a method in which the inlet for the carrier gas is provided above the surface of the reactive liquid in the reactive liquid container, and a method in which the inlet port is provided below the liquid surface.

前者すなわちガス導入口を液面上に設ける場合
はガス導入口およびキヤリアガスに担持された反
応性液体の蒸気の排出口と液面との距離が残留液
量により変り、また容器断面が高さにより異る場
合、気液界面の面積が残留液量により変ることと
なる。このため温度、キヤリアガス流量を同じに
しても残留液量により蒸発速度が異るため液体蒸
気の濃度が異つたり、また蒸気の取り込みかたが
変るため同様に濃度が異ることとなり、得られる
単結晶の組成、不純物濃度あるいは拡散層の不純
物濃度等の再現性がよくないという問題があつ
た。
In the former case, where the gas inlet is provided above the liquid level, the distance between the gas inlet and the outlet for the vapor of the reactive liquid supported by the carrier gas and the liquid level will vary depending on the amount of remaining liquid, and the cross-section of the container will vary depending on the height. If they are different, the area of the gas-liquid interface will change depending on the amount of residual liquid. Therefore, even if the temperature and carrier gas flow rate are the same, the evaporation rate will differ depending on the amount of residual liquid, resulting in a different concentration of liquid vapor, and the method of taking in the vapor will also change, resulting in a similar concentration difference. There was a problem in that the reproducibility of the single crystal composition, impurity concentration, impurity concentration of the diffusion layer, etc. was not good.

後者すなわちガス導入口を液面下に設け、キヤ
リアガスを液体内に泡出させる場合は、上記とほ
ぼ同様に残留液量により液面が変ることによる再
現性の不良の問題の他に、次のような問題が生ず
る。すなわち導入口から出たキヤリアガスの泡が
液面上等で潰れる際の飛沫が微小な液滴として一
部は反応容器まで、また一部はガス配管部まで輸
送されて管壁に付着したりする。管壁等の温度は
通常制御されないので、これらの蒸気量が雰囲気
温度により変り、上記と同様に再現性の不良の問
題を生ずる。また管壁に付着した液体が分解して
粉末状の物が析出したり、酸化物が析出したりし
て悪影響を及ぼす。
In the latter case, in which the gas inlet is provided below the liquid surface and the carrier gas is bubbled into the liquid, in addition to the problem of poor reproducibility due to changes in the liquid level depending on the amount of remaining liquid, as well as the following problems: Problems like this arise. In other words, when the carrier gas bubbles emitted from the inlet collapse on the liquid surface, some of the droplets are transported as minute droplets to the reaction vessel, and some of them are transported to the gas piping section and adhere to the pipe wall. . Since the temperature of the tube walls etc. is usually not controlled, the amount of these vapors changes depending on the ambient temperature, causing the same problem of poor reproducibility as described above. In addition, the liquid adhering to the tube wall decomposes and precipitates powder or oxides, which has an adverse effect.

〔発明の目的〕[Purpose of the invention]

本発明はこれらの欠点を解決するためになされ
たもので、その目的は排出口からのキヤリアガス
中に含まれる液体蒸気の濃度の制御性、再現性を
改善し得る反応性液体容器を提供することにあ
る。また他の目的は容器内の液体残量を容易に認
知できる反応性液体容器を提供することにある。
The present invention has been made to solve these drawbacks, and its purpose is to provide a reactive liquid container that can improve the controllability and reproducibility of the concentration of liquid vapor contained in the carrier gas from the outlet. It is in. Another object of the present invention is to provide a reactive liquid container in which the remaining amount of liquid in the container can be easily determined.

〔発明の構成〕[Structure of the invention]

前記目的を達成する本発明について概説する
と、本発明はキヤリアガスの導入口とキヤリアガ
スに担持された反応性液体の蒸気の排出口とを設
けた反応性液体容器において、容器内が隔壁で第
1帯域と第2帯域に分割され、第1帯域と第2帯
域とは隔壁の下部において連通すると共に第1帯
域に前記導入口と排出口を設けたことを特徴とす
る反応性液体容器(第1発明)およびキヤリアガ
スの導入口とキヤリアガスに担持された反応性液
体の蒸気の排出口とを設けた反応性液体容器にお
いて、容器内が隔壁で第1帯域と第2帯域に分割
され、第1帯域と第2帯域とは隔壁の下部におい
て連通すると共に第1帯域に前記導入口と排出口
を設け、第2帯域に該帯域の気圧を表示する圧力
計を設けたことを特徴とする反応性液体容器(第
2発明)に関する。そして本発明は前記構成によ
り、容器内の反応性液体が蒸発する気液界面を第
1帯域に設定し、その気液界面の位置を一定に保
つことを可能にしたものである。
To summarize the present invention that achieves the above object, the present invention provides a reactive liquid container provided with an inlet for a carrier gas and an outlet for the vapor of a reactive liquid carried by the carrier gas, wherein the interior of the container is a partition wall and a first zone is formed. and a second zone, the first zone and the second zone communicate with each other at the lower part of the partition wall, and the first zone is provided with the inlet and the outlet. ) and a reactive liquid container provided with a carrier gas inlet and an outlet for the vapor of the reactive liquid carried by the carrier gas, the interior of the container is divided by a partition into a first zone and a second zone, and the first zone and A reactive liquid container that communicates with the second zone at the lower part of the partition, the first zone being provided with the inlet and the outlet, and the second zone being provided with a pressure gauge for displaying the atmospheric pressure of the zone. (Second invention). With the above configuration, the present invention makes it possible to set the gas-liquid interface where the reactive liquid in the container evaporates in the first zone, and to keep the position of the gas-liquid interface constant.

次に本発明の反応性液体容器の構成を図面を参
照して説明する。第1図は本発明の反応性液体容
器の一実施例の断面図を示す。容器1内に反応性
液体(以下単に液体という。)2が収容されてい
る。3は容器内にキヤリアガスを導入するための
管、4は液体の蒸気とともにキヤリアガスを排出
するための管である。容器内は隔壁5によりガス
導入管3および排出管4を具備した第1帯域6と
外界と遮断された第2帯域7に分割されており、
各帯域6と7は図に示すように隔壁5の下部にお
いて連通されている。この連通のためには図に示
すように隔壁5を容器の長さより短かくしてもよ
く、また隔壁の一部に貫通孔を設けてもよい。
Next, the configuration of the reactive liquid container of the present invention will be explained with reference to the drawings. FIG. 1 shows a cross-sectional view of one embodiment of the reactive liquid container of the present invention. A reactive liquid (hereinafter simply referred to as liquid) 2 is contained in a container 1 . 3 is a pipe for introducing carrier gas into the container, and 4 is a pipe for discharging the carrier gas together with liquid vapor. The inside of the container is divided by a partition wall 5 into a first zone 6 equipped with a gas introduction pipe 3 and a discharge pipe 4, and a second zone 7 cut off from the outside world.
Each zone 6 and 7 communicates at the lower part of the partition wall 5 as shown. For this communication, the partition wall 5 may be made shorter than the length of the container as shown in the figure, or a through hole may be provided in a part of the partition wall.

キヤリアガスに担持されて液体の蒸気が排出さ
れ、液体が蒸発すると第1帯域における液面8が
下がり、第1帯域と第2帯域の連通部より下がる
とガスが第2帯域7に入り、第1帯域の液面が上
がる。すなわち液面8の位置は連通部の最上端部
(隔壁5の下端)附近にほぼ固定される。したが
つて、液体残量の変化に伴う液面位置の変化、液
面の表面積の変化を伴う問題を避けることがで
き、液体の温度とキヤリアガスの流量を制御する
だけで所望の液体の蒸気を再現性よく排出するこ
とができる。
The vapor of the liquid supported by the carrier gas is discharged, and when the liquid evaporates, the liquid level 8 in the first zone falls, and when it falls below the communication part between the first zone and the second zone, the gas enters the second zone 7, and the liquid level 8 in the first zone falls. The liquid level in the band rises. That is, the position of the liquid level 8 is substantially fixed near the uppermost end of the communication portion (lower end of the partition wall 5). Therefore, problems associated with changes in the liquid level position and surface area due to changes in the remaining amount of liquid can be avoided, and the desired liquid vapor can be generated simply by controlling the liquid temperature and carrier gas flow rate. It can be discharged with good reproducibility.

9は容器の洗浄、液体の補充等のために設けた
穴でネジ部10により密閉された場合を示すもの
であるが、これらの構成は本発明の作用に影響す
るものではなく、単に容器の底部の構造の1具体
例を述べたにとどまるものである。
Reference numeral 9 indicates a hole provided for cleaning the container, replenishing liquid, etc., and is sealed by a threaded portion 10. However, these configurations do not affect the operation of the present invention, and merely improve the effectiveness of the container. This is merely a specific example of the bottom structure.

この容器に液体を充填するには容器内を適度に
真空排気しておき、しかる後液体を吸入させるこ
とにより行なうことができる。所望の量の液体を
入れた後、キヤリアガスと同種のガスまたは不活
性ガス等を導入すれば図に示すような液面位置の
差をつくることができる。
This container can be filled with liquid by evacuating the inside of the container to an appropriate degree and then sucking in the liquid. After adding the desired amount of liquid, by introducing a gas of the same type as the carrier gas or an inert gas, it is possible to create a difference in the liquid level position as shown in the figure.

第2図は本発明の他の実施例であつて、上記説
明した容器の第2帯域7の上部ガス充填部分の内
圧を測定表示するための圧力計11を設けた容器
の断面図を示す。第2帯域7の内圧は第1帯域6
よりも液面の高さの差分だけ圧力が下がるのでそ
の圧力を知ることにより液体残量を知ることがで
きる。これをより正確に行うには第1帯域と第2
帯域の差圧を表示するようにすればよい。この差
圧はρghで与えられる。ここでρは液体の密度、
gは重力加速度、hは液面の高さである。
FIG. 2 shows another embodiment of the present invention, which is a sectional view of a container provided with a pressure gauge 11 for measuring and displaying the internal pressure of the upper gas-filled portion of the second zone 7 of the container described above. The internal pressure of the second zone 7 is the same as that of the first zone 6.
The pressure decreases by the difference in the height of the liquid level, so by knowing the pressure, you can know the remaining amount of liquid. To do this more accurately, the first and second bands
What is necessary is to display the differential pressure in the band. This differential pressure is given by ρgh. Here ρ is the density of the liquid,
g is the gravitational acceleration and h is the height of the liquid level.

図中、キヤリアガス導入管3の先端が第2帯域
7内の液面より下になるように示してあるが、こ
れよりも短かく、極端には排気管と同様容器内に
突出しなくてもよい。また一方排気管が容器内に
延長して設けられてもよい。
In the figure, the tip of the carrier gas introduction pipe 3 is shown to be below the liquid level in the second zone 7, but it may be shorter than this, and in the extreme it does not need to protrude into the container like the exhaust pipe. . Alternatively, an exhaust pipe may be provided extending into the container.

容器に収容する反応性液体はその利用分野によ
り異なるが、例えばシリコンの酸化に使用する水
でもよく、通常の状態で極めて反応性が強い必要
はない。
The reactive liquid contained in the container varies depending on its field of use, but may be water used for oxidizing silicon, for example, and does not need to be extremely reactive under normal conditions.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明においては容器内
に隔壁を設けて2帯域に分割し、キヤリアガスの
導入口、液体蒸気の排出口をその一方に集めるこ
とにより以下のような効果を達成できる。
As explained above, in the present invention, the following effects can be achieved by providing a partition inside the container to divide it into two zones, and concentrating the carrier gas inlet and liquid vapor outlet in one of the zones.

第1の効果は液体残量の多少にかかわらず液面
の高さを一定に維持でき、キヤリアガス導入口、
および排出口と液面の位置関係を一定にできる。
この結果この容器から排出するキヤリアガス中の
液体蒸気濃度は液体の温度とキヤリアガス流量の
みで定まり、再現性よく制御することができる。
The first effect is that the liquid level can be maintained constant regardless of the amount of liquid remaining, and the carrier gas inlet
Also, the positional relationship between the discharge port and the liquid level can be kept constant.
As a result, the liquid vapor concentration in the carrier gas discharged from the container is determined only by the temperature of the liquid and the flow rate of the carrier gas, and can be controlled with good reproducibility.

第2の効果はこのような容器に圧力計を附加す
ることにより、液体残量を容易に知ることができ
る。金属製等の内部を直視できない容器において
効果が著るしい。
The second effect is that by adding a pressure gauge to such a container, the remaining amount of liquid can be easily determined. The effect is most noticeable in containers made of metal or other materials whose interior cannot be viewed directly.

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

第1図および第2図は本発明の一実施例の断面
図を示す。 1……容器、2……反応性液体、3……キヤリ
アガス導入管、4……排出管、5……隔壁、6…
…第1帯域、7……第2帯域、8……液面、11
……圧力計。
1 and 2 show cross-sectional views of one embodiment of the invention. DESCRIPTION OF SYMBOLS 1... Container, 2... Reactive liquid, 3... Carrier gas introduction pipe, 4... Discharge pipe, 5... Partition wall, 6...
...First zone, 7...Second zone, 8...Liquid level, 11
...Pressure gauge.

Claims (1)

【特許請求の範囲】 1 キヤリアガスの導入口とキヤリアガスに担持
された反応性液体の蒸気の排出口とを設けた反応
性液体容器において、容器内が隔壁で第1帯域と
第2帯域に分割され、第1帯域と第2帯域とは隔
壁の下部において連通すると共に第1帯域に前記
導入口と排出口を設けたことを特徴とする反応性
液体容器。 2 キヤリアガスの導入口とキヤリアガスに担持
された反応性液体の蒸気の排出口とを設けた反応
性液体容器において、容器内が隔壁で第1帯域と
第2帯域に分割され、第1帯域と第2帯域とは隔
壁の下部において連通すると共に第1帯域に前記
導入口と排出口を設け、第2帯域に該帯域の気圧
を表示する圧力計を設けたことを特徴とする反応
性液体容器。
[Claims] 1. A reactive liquid container provided with an inlet for a carrier gas and an outlet for vapor of a reactive liquid carried by the carrier gas, in which the inside of the container is divided by a partition into a first zone and a second zone. A reactive liquid container, characterized in that the first zone and the second zone communicate with each other at the lower part of the partition wall, and the first zone is provided with the inlet and the outlet. 2. In a reactive liquid container provided with an inlet for a carrier gas and an outlet for vapor of a reactive liquid carried by the carrier gas, the inside of the container is divided by a partition into a first zone and a second zone, and the interior of the container is divided into a first zone and a second zone. A reactive liquid container, characterized in that the two zones communicate with each other at the lower part of the partition wall, the first zone is provided with the inlet and the outlet, and the second zone is provided with a pressure gauge that displays the atmospheric pressure of the zone.
JP6220183A 1983-04-11 1983-04-11 Reactive liquid container Granted JPS59189932A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6220183A JPS59189932A (en) 1983-04-11 1983-04-11 Reactive liquid container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6220183A JPS59189932A (en) 1983-04-11 1983-04-11 Reactive liquid container

Publications (2)

Publication Number Publication Date
JPS59189932A JPS59189932A (en) 1984-10-27
JPH0252537B2 true JPH0252537B2 (en) 1990-11-13

Family

ID=13193291

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6220183A Granted JPS59189932A (en) 1983-04-11 1983-04-11 Reactive liquid container

Country Status (1)

Country Link
JP (1) JPS59189932A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2001286404A1 (en) * 2000-08-04 2002-02-18 Arch Specialty Chemicals, Inc. Automatic refill system for ultra pure or contamination sensitive chemicals
US8440139B2 (en) 2004-03-04 2013-05-14 Ethican, Inc. Method of delivering liquid sterilant to a sterilizer
JP4558538B2 (en) * 2004-03-04 2010-10-06 エシコン・インコーポレイテッド Method for delivering liquid sterilant to sterilizer

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JPS59189932A (en) 1984-10-27

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