JPH0351313Y2 - - Google Patents

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Publication number
JPH0351313Y2
JPH0351313Y2 JP4592886U JP4592886U JPH0351313Y2 JP H0351313 Y2 JPH0351313 Y2 JP H0351313Y2 JP 4592886 U JP4592886 U JP 4592886U JP 4592886 U JP4592886 U JP 4592886U JP H0351313 Y2 JPH0351313 Y2 JP H0351313Y2
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JP
Japan
Prior art keywords
raw material
pipe
material container
auxiliary
liquid
Prior art date
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Expired
Application number
JP4592886U
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Japanese (ja)
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JPS62157940U (en
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Priority to JP4592886U priority Critical patent/JPH0351313Y2/ja
Publication of JPS62157940U publication Critical patent/JPS62157940U/ja
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  • Glass Melting And Manufacturing (AREA)
  • Manufacture, Treatment Of Glass Fibers (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

【考案の詳細な説明】 『産業上の利用分野』 本考案は原料消費にともなう主原料容器内の原
料減少を補償すべく、補助原料容器内の原料を主
原料容器内へ補給するための装置に関する。
[Detailed description of the invention] "Field of industrial application" This invention is a device for replenishing the raw material in the auxiliary raw material container into the main raw material container in order to compensate for the decrease in raw material in the main raw material container due to raw material consumption. Regarding.

『従来技術とその問題点』 通信分野、光学分野等において高純度かつ高品
位のガラス材をMCVD法、PCVD法、VAD法、
OVD法など、適宜の手段で作製するとき、主原
料容器からの気化原料を所定の反応系へ供給し、
この際の原料消費にともなう主原料容器内の原料
減少を、補助原料容器内から主原料容器内への原
料補給により補償している。
"Prior art and its problems" High purity and high quality glass materials are manufactured using the MCVD method, PCVD method, VAD method, etc. in the communication field, optical field, etc.
When producing by an appropriate method such as OVD method, the vaporized raw material from the main raw material container is supplied to a predetermined reaction system,
At this time, the decrease in the raw material in the main raw material container due to raw material consumption is compensated for by replenishing the raw material from the auxiliary raw material container into the main raw material container.

かかる原料補給装置として、特開昭60−122735
号公報に開示の先行技術が一般に使用されていた
が、この装置は同号の発明が指摘するように種々
の問題がみられる。
As such a raw material replenishment device, Japanese Patent Application Laid-Open No. 60-122735
Although the prior art disclosed in the above publication has been commonly used, this device suffers from various problems as pointed out by the invention of the same publication.

これを改善した特開昭60−122735号公報の発明
では、補助原料容器に設けられたガス圧送用の配
管系と、補助原料容器から主原料容器にわたる液
体原料補給用の配管系とを巧みに組み合わせるこ
とにより、補助原料容器内から主原料容器内への
原料補給を効率よく行なうようにしたが、この従
来発明をしても各配管系の合理的構成、原料補給
管内に残留液体原料の円滑な処理につき、改善の
余地が残されている。
The invention disclosed in Japanese Patent Application Laid-Open No. 122735/1983 improves this by skillfully connecting the gas pressure feeding piping system provided in the auxiliary raw material container and the liquid raw material replenishment piping system from the auxiliary raw material container to the main raw material container. By combining these, it is possible to efficiently replenish raw materials from the auxiliary raw material container to the main raw material container. However, even with this conventional invention, it is difficult to rationally configure each piping system and smoothly remove the remaining liquid raw material in the raw material supply pipe. There is still room for improvement regarding processing.

本考案は上記の問題点に鑑み、原料補給用の配
管系を合理化し、しかも、原料補給管内に残留す
る液体原料が円滑に処理できる原料補助装置を提
供しようとするものである。
In view of the above-mentioned problems, the present invention aims to provide a raw material auxiliary device that can streamline the raw material replenishment piping system and can smoothly dispose of the liquid raw material remaining in the raw material supply pipe.

『問題点を解決するための手段』 本考案は所期の目的を達成するため、内部の液
体原料を気化してその気化原料を外部へ取り出す
主原料容器内に、原料補給用の配管系を介して補
助原料容器内の液体原料を補給する装置におい
て、液体原料を収容した密閉型の上記補助原料容
器はガス吹込管、原料補給管、大気連通用配管、
補助配管を備え、上記ガス吹込管は、その管路中
に制御弁を有して補助原料容器の気相部に挿入さ
れており、制御弁を有する両端の縦管部と、これ
ら両縦管部にわたる横管部とからなる上記原料補
給管は、その一方の縦管部が補助原料容器内に、
その他方の縦管部が主原料容器内にそれぞれ挿入
されているとともに、その横管部が主原料容器側
から補助原料容器側に向けて下降する勾配を有
し、上記大気連通用配管は、その管路中に制御弁
を有して補助原料容器の気相部に挿入されてお
り、上記補助配管は、その管路中に制御弁を有し
てその一端がガス吹込管に、その他端が原料補給
管の最高位部にそれぞれ接続されていることを特
徴とする。
``Means for Solving Problems'' In order to achieve the intended purpose, this invention has a piping system for replenishing raw materials inside the main raw material container that vaporizes the liquid raw materials inside and takes out the vaporized raw materials to the outside. In the apparatus for replenishing the liquid raw material in the auxiliary raw material container through a gas blowing pipe, a raw material supply pipe, a pipe for communicating with the atmosphere,
The gas blowing pipe has a control valve in the pipe and is inserted into the gas phase part of the auxiliary raw material container, and has vertical pipe parts at both ends having control valves, and both vertical pipes. The above-mentioned raw material supply pipe consists of a horizontal pipe part extending over 300 mm, and one of the vertical pipe parts is inside the auxiliary raw material container,
The other vertical pipe part is inserted into the main raw material container, and the horizontal pipe part has a slope that descends from the main raw material container side to the auxiliary raw material container side, and the atmospheric communication piping is The auxiliary pipe has a control valve in the pipe and is inserted into the gas phase part of the auxiliary raw material container, and the auxiliary pipe has a control valve in the pipe, one end of which is connected to the gas blowing pipe, and the other end of which is inserted into the gas phase part of the auxiliary raw material container. are connected to the highest parts of the raw material supply pipes.

『作用』 上述した本考案装置では、主原料容器内におけ
る液体原料の減少量が所定値となつたとき、ガス
吹込管を介して補助原料容器内を加圧し、これに
より補助原料容器内の液体原料を主原料容器内へ
圧送する。
``Operation'' In the device of the present invention described above, when the amount of decrease in the liquid raw material in the main raw material container reaches a predetermined value, the inside of the auxiliary raw material container is pressurized via the gas blowing pipe, thereby reducing the liquid in the auxiliary raw material container. The raw material is pumped into the main raw material container.

かかる原料補給により主原料容器内の液体原料
が所定量となつたとき、ガス吹込管による補助原
料容器内の加圧を停止すると同時に大気連通用配
管を開放し、しかも、該ガス吹込管のガスを補助
配管経由により原料補給管へ流し、これにより原
料補給管内に残留している液体原料の一部を補助
原料容器内へ返送し、その残部を主原料容器内へ
送りこむ。
When the liquid raw material in the main raw material container reaches a predetermined amount by such raw material replenishment, pressurization of the auxiliary raw material container by the gas blowing pipe is stopped, and at the same time, the atmosphere communication pipe is opened, and the gas in the gas blowing pipe is is flowed into the raw material supply pipe via the auxiliary pipe, whereby a part of the liquid raw material remaining in the raw material supply pipe is returned to the auxiliary raw material container, and the remainder is sent into the main raw material container.

したがつて、原料補給後の原料補給管内に液体
原料が残留することがなく、その原料残留がない
ことにより、補助原料容器内から主原料容器内へ
の液体原料補給が常に正確に行なえる。
Therefore, no liquid raw material remains in the raw material replenishment pipe after the raw material is replenished, and because there is no residual raw material, the liquid raw material can always be accurately replenished from the auxiliary raw material container to the main raw material container.

この際、補助原料容器内は大気連通用配管を介
して大気と連通するから、原料補給管内に残留の
液体原料は圧力抵抗を受ず、しかも、原料補給管
の横管部が主原料容器側から補助原料容器側に向
けて下降する勾配を有するから、かかるヘツド差
と上記ガス圧との相乗効果により原料補給管内に
残留の液体原料は速やかに補助原料容器内に返送
される。
At this time, the inside of the auxiliary raw material container is communicated with the atmosphere via the atmosphere communication pipe, so the liquid raw material remaining in the raw material supply pipe does not experience pressure resistance, and moreover, the horizontal pipe part of the raw material supply pipe is on the side of the main raw material container. Since it has a slope that descends from the top to the side of the auxiliary raw material container, the liquid raw material remaining in the raw material supply pipe is quickly returned to the auxiliary raw material container due to the synergistic effect of the head difference and the gas pressure.

その上、必要な配管がガス吹込管、原料補給
管、大気連通用配管、補助配管などで足りるか
ら、総体的な配管系が簡略かつ安価に構成でき
る。
Furthermore, since the necessary piping is a gas blowing pipe, a raw material supply pipe, an atmospheric communication pipe, an auxiliary pipe, etc., the overall piping system can be constructed simply and inexpensively.

『実施例』 以下、本考案に係る原料補給装置の実施例につ
き、図面を参照して説明する。
"Embodiments" Hereinafter, embodiments of the raw material replenishment device according to the present invention will be described with reference to the drawings.

第1図において、21は既知の恒温槽、31は
主原料容器、41は液面計、51は流路制御器、
61は補助原料容器である。
In FIG. 1, 21 is a known constant temperature bath, 31 is a main raw material container, 41 is a liquid level gauge, 51 is a flow path controller,
61 is an auxiliary raw material container.

恒温槽21内に装填された主原料容器31は、
その内部の下位に液体原料を収容した液相部32
を有するとともに、その内部の上位に気化原料に
よる気相部33を有し、液相部32にはキヤリア
ガス吹込管34が挿入され、気相部33には反応
系に通じる気化原料取出管35が挿入されてい
る。
The main raw material container 31 loaded into the constant temperature bath 21 is
Liquid phase section 32 containing liquid raw material in the lower part thereof
It also has a gas phase part 33 containing vaporized raw materials in the upper part thereof, a carrier gas blowing pipe 34 is inserted into the liquid phase part 32, and a vaporized raw material extraction pipe 35 communicating with the reaction system is inserted into the gas phase part 33. It has been inserted.

キヤリアガス吹込管34は図示しないガスボン
ベに接続され、その管路上に流量制御器36、制
御弁37を有する。
The carrier gas blowing pipe 34 is connected to a gas cylinder (not shown), and has a flow rate controller 36 and a control valve 37 on the pipe.

気化原料取出管35はその管路中に制御弁38
を有する。
The vaporized raw material extraction pipe 35 has a control valve 38 in its pipe line.
has.

液面計41は主原料容器31の液相部32、気
相部33と連通する細管構造を主体にし、これに
主原料容器31内の液面位を流路制御器51へ報
知する検出機構が組み合わされている。
The liquid level gauge 41 mainly has a thin tube structure that communicates with the liquid phase part 32 and the gas phase part 33 of the main raw material container 31, and has a detection mechanism that notifies the liquid level inside the main raw material container 31 to the flow path controller 51. are combined.

流路制御器51は液面計41を介して原料容器
31の所定液面範囲を検出すべき二つのセンサ5
2,53を備え、これらセンサ52,53が液面
計41の所定位置に対応して配置されている。
The flow path controller 51 has two sensors 5 to detect a predetermined liquid level range of the raw material container 31 via a liquid level gauge 41.
2 and 53, and these sensors 52 and 53 are arranged corresponding to predetermined positions of the liquid level gauge 41.

補助原料容器61は、その内部の下位に液体原
料を収容した液相部62を、その内部の上位に気
相部63をそれぞれ有し、かつ、所定の配管とし
て、ガス吹込管64,原料補給管65、大気連通
用配管66、補助配管67などが設備されてい
る。
The auxiliary raw material container 61 has a liquid phase part 62 containing a liquid raw material in the lower part thereof, and a gas phase part 63 in the upper part thereof, and has a gas blowing pipe 64 and a raw material supply pipe as predetermined piping. A pipe 65, an atmosphere communication pipe 66, an auxiliary pipe 67, and the like are provided.

ガス吹込管64は、図示しないガスボンベに接
続されているとともに、その管路中に制御弁68
を有し、かかるガス吹込管64は補助原料容器6
1の気相部63に挿入されている。
The gas blowing pipe 64 is connected to a gas cylinder (not shown), and a control valve 68 is provided in the pipe.
The gas blowing pipe 64 is connected to the auxiliary raw material container 6.
It is inserted into the gas phase section 63 of No. 1.

原料補給管65は、制御弁69を有する縦管部
65aと、制御弁70,71を有する縦管部65
cと、これら両縦管部65a,65cにわたる傾
斜状の横管部65bとからなり、一方の縦管部6
5aが補助原料容器61の液相部62に挿入さ
れ、他方の縦管部65cが主原料容器31の気相
部33に挿入されている。
The raw material supply pipe 65 includes a vertical pipe part 65a having a control valve 69 and a vertical pipe part 65 having control valves 70 and 71.
c, and an inclined horizontal tube portion 65b spanning both vertical tube portions 65a and 65c, with one vertical tube portion 6
5a is inserted into the liquid phase part 62 of the auxiliary raw material container 61, and the other vertical pipe part 65c is inserted into the gas phase part 33 of the main raw material container 31.

原料補給管65の横管部65bが上記のごとき
傾斜状態を呈しているとき、相対的に縦管部65
cの上端が高く、縦管部65aの上端が低い。
When the horizontal pipe portion 65b of the raw material supply pipe 65 is inclined as described above, the vertical pipe portion 65
The upper end of the vertical pipe portion 65a is high, and the upper end of the vertical tube portion 65a is low.

制御弁72を備えた大気連通用配管66は、そ
の一端が補助原料容器61の気相部63に挿入さ
れているとともに、制御弁72を開放することに
よりその他端が大気と連通するようになつてい
る。
The atmosphere communication pipe 66 equipped with a control valve 72 has one end inserted into the gas phase section 63 of the auxiliary raw material container 61, and the other end communicates with the atmosphere by opening the control valve 72. ing.

補助配管67は、その管路中に制御弁73を有
し、その一端がガス吹込管64に接続されている
とともに、その他端が原料補給管65の最高位部
に接続されている。
The auxiliary pipe 67 has a control valve 73 in its pipe line, and one end thereof is connected to the gas blowing pipe 64, and the other end is connected to the highest part of the raw material supply pipe 65.

上述した各配管の制御弁37,38,68,6
9,70,71,72,73は、例えば電磁弁の
ごとく電気的に制御可能なものからなり、流路制
御器51を介して開閉操作できるようになつてい
る。
Control valves 37, 38, 68, 6 for each piping described above
The valves 9, 70, 71, 72, and 73 are electrically controllable, such as electromagnetic valves, and can be opened and closed via the flow path controller 51.

第1図の実施例において、気化原料を所定の反
応系へ供給する際の定常運転時、制御弁37,3
8が開状態、他の制御弁68,69,70,7
1,72,73が閉状態に保持される。
In the embodiment shown in FIG. 1, during steady operation when supplying vaporized raw materials to a predetermined reaction system, the control valves
8 is open, other control valves 68, 69, 70, 7
1, 72, and 73 are held closed.

この定常運転では、不活性ガス(例えばAr)
あるいは酸素などのキヤリアガスが、キヤリアガ
ス吹込管34を介して主原料容器31の液相部3
2に吹きこまれるとともに、この際のバブリング
作用により気化され、キヤリアガスにより担持さ
れた原料が、主原料容器31の気相部33から気
化原料取出管35を介して所定の反応系へ給送さ
れる。
In this steady-state operation, inert gas (e.g. Ar)
Alternatively, a carrier gas such as oxygen is supplied to the liquid phase portion 3 of the main raw material container 31 via the carrier gas blowing pipe 34.
2, the raw material is vaporized by the bubbling action at this time and supported by the carrier gas, and is fed from the gas phase section 33 of the main raw material container 31 to a predetermined reaction system via the vaporized raw material take-out pipe 35. Ru.

上記気化原料供給により主原料容器31内の液
体原料は減少するが、その減少量が所定値となつ
たとき、液面計41から流路制御器51へ所定の
検知信号が入力され、当該検知信号を受けた流路
制御器51が制御弁37,72,73を閉状態、
他の制御弁38,68,69,70,71を開状
態にする。
The liquid raw material in the main raw material container 31 decreases due to the supply of the vaporized raw material, but when the amount of decrease reaches a predetermined value, a predetermined detection signal is input from the liquid level gauge 41 to the flow path controller 51, and the corresponding detection signal is input to the flow path controller 51. Upon receiving the signal, the flow path controller 51 closes the control valves 37, 72, and 73,
The other control valves 38, 68, 69, 70, 71 are opened.

かかる状態のとき、ガス吹込管64から補助原
料容器61内の気相部63に不活性ガス(例えば
N2)が圧入され、そのガス圧により加圧された
補助原料容器61内の液体原料(液相部62)
が、原料補給管65の縦管部65a、横管部65
b、縦管部65cを経て主原料容器31内へ補給
される。
In such a state, an inert gas (for example,
The liquid raw material (liquid phase part 62) in the auxiliary raw material container 61 is pressurized by the gas pressure.
However, the vertical pipe part 65a and the horizontal pipe part 65 of the raw material supply pipe 65
b, it is replenished into the main raw material container 31 through the vertical pipe portion 65c.

原料補給により主原料容器31内の液体原料が
所定の増加量となつたとき、液面計41を監視し
ている一方のセンサ52がこれを検知してその検
知信号を流路制御器51へ入力し、当該検知信号
を受けた流路制御器51は、制御弁68を閉状
態、制御弁72,73を開状態にする。
When the liquid raw material in the main raw material container 31 reaches a predetermined amount due to raw material replenishment, one sensor 52 monitoring the liquid level gauge 41 detects this and sends the detection signal to the flow path controller 51. The flow path controller 51 that receives the input and the detection signal closes the control valve 68 and opens the control valves 72 and 73.

制御弁68の閉止状態では補助原料容器61内
は加圧されず、したがつて、補助原料容器61→
原料補給管65→主原料容器31の原料補給は止
まる。
When the control valve 68 is closed, the inside of the auxiliary raw material container 61 is not pressurized, so that the auxiliary raw material container 61→
The supply of raw materials from the raw material supply pipe 65 to the main raw material container 31 is stopped.

一方、上記制御弁68の閉止にともない、ガス
吹込管64から不活性ガスは補助配管67を通
り、かつ、横管部65b,縦管部65cの分岐箇
所からその両方へ分流する。
On the other hand, as the control valve 68 is closed, the inert gas from the gas blowing pipe 64 passes through the auxiliary pipe 67 and is branched to both the horizontal pipe part 65b and the vertical pipe part 65c from the branching point.

その結果、原料補給管65の横管部65bおよ
び縦管部65aに残留している液体原料が補助原
料容器61内へ返送されるとともに、原料補給管
65の縦管部65cに残留している液体原料が主
原料容器31内へ送りこまれ、かくて原料補給管
65内の液体原料残留が防止できる。
As a result, the liquid raw material remaining in the horizontal pipe part 65b and vertical pipe part 65a of the raw material supply pipe 65 is returned to the auxiliary raw material container 61, and remains in the vertical pipe part 65c of the raw material supply pipe 65. The liquid raw material is fed into the main raw material container 31, thus preventing the liquid raw material from remaining in the raw material supply pipe 65.

特に原料補給管65の横管部65bは、これが
補助原料容器61側へ下降傾斜しているので、そ
の管部内の残留液体原料がより速やかに補助原料
容器61へ返送される。
In particular, the horizontal pipe portion 65b of the raw material supply pipe 65 is inclined downward toward the auxiliary raw material container 61, so that the remaining liquid raw material in the pipe portion is returned to the auxiliary raw material container 61 more quickly.

上記において、原料補給管65の縦管部65c
に残留している液体原料が主原料容器31内へ送
りこまれたとき、その分だけ主原料容器31内の
液面位が上昇するが、この際の量は既知量である
から、液面計41を監視している他方のセンサ5
3を設定する際、あらかじめ考慮しておけばよ
い。
In the above, the vertical pipe portion 65c of the raw material supply pipe 65
When the remaining liquid raw material is sent into the main raw material container 31, the liquid level in the main raw material container 31 rises by that amount, but since the amount at this time is a known amount, the liquid level meter The other sensor 5 monitoring 41
3 should be taken into consideration in advance.

ただし実際上、この残留分は、総補給量に対し
てごくわずかな量であるため無視できる。
However, in reality, this residual amount is negligible compared to the total supply amount, so it can be ignored.

なお、一つの補助原料容器61から複数の主原
料容器31へ液体原料を補給するとき、図の二点
鎖線で囲う配管構成を、原料補給管65、補助配
管67にわたつて複数組設け、その際の縦管部6
5cを各主原料容器31内に挿入すればよい。
In addition, when replenishing liquid raw materials from one auxiliary raw material container 61 to a plurality of main raw material containers 31, multiple sets of the piping configuration surrounded by the two-dot chain line in the figure are provided across the raw material supply pipe 65 and the auxiliary piping 67. Vertical tube part 6
5c into each main raw material container 31.

補助原料容器61:主原料容器31が「1:複
数」の場合も、補助原料容器61から各主原料容
器31への原料補給は前記と同様に行なわれ、各
主原料容器31への原料補給の停止に際しては、
該各主原料容器31のセンサ53が所定液面位を
検知した順に、前記と同様の残留液返送動作が行
なわれる。
Even when the number of auxiliary raw material containers 61:main raw material containers 31 is "1:multiple", raw material replenishment from the auxiliary raw material container 61 to each main raw material container 31 is performed in the same manner as described above, and raw material replenishment to each main raw material container 31 is performed in the same manner as described above. When stopping,
The same residual liquid return operation as described above is performed in the order in which the sensor 53 of each main raw material container 31 detects a predetermined liquid level.

補助原料容器61から各主原料容器31への原
料補給手段として、第2図のように、原料補給管
65にポンプ82付の配管81を接続するなど、
他の液送手段も採用できるが、かかる場合も前記
と同様、ガス圧送により原料補給管65内の残留
液体原料の排除が行なわれる。
As a means for supplying raw materials from the auxiliary raw material container 61 to each main raw material container 31, as shown in FIG. 2, a pipe 81 with a pump 82 is connected to the raw material supply pipe 65.
Other liquid feeding means may also be employed, but in such a case as well, the remaining liquid raw material in the raw material supply pipe 65 is removed by gas pressure feeding, as described above.

制御弁70,71は、これらのいずれか一方を
省略してもよい。
Either one of the control valves 70 and 71 may be omitted.

『考案の効果』 以上説明した通り、本考案装置によるときは、
補助原料容器から主原料容器内へ液体原料を補給
するための配管系を、ガス吹込管、原料補給管、
大気連通用配管、補助配管により有機的に配管構
成したから、原料補給後の原料補給管内に液体原
料が残留することがなく、補助原料容器内から主
原料容器内への液体原料補給が常に正確に行なえ
るとともに、原料補給管内に残留の液体原料も速
やかに処理でき、しかも、総体的な配管系が上記
各管により簡略かつ安価に構成できる。
``Effect of the invention'' As explained above, when using the device of the present invention,
The piping system for replenishing liquid raw materials from the auxiliary raw material container into the main raw material container includes gas blowing pipes, raw material supply pipes,
Because the piping is organically configured with atmospheric communication piping and auxiliary piping, there is no residual liquid in the raw material replenishment pipe after replenishing the raw material, and liquid raw material can always be accurately replenished from the auxiliary raw material container to the main raw material container. In addition, the liquid raw material remaining in the raw material supply pipe can be quickly disposed of, and the overall piping system can be constructed simply and inexpensively using the above-mentioned pipes.

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

第1図は本考案に係る原料補給装置の一実施例
を略示した説明図、第2図は同上の他実施例を略
示した説明図である。 31……主原料容器、61……補助原料容器、
62……補助原料容器の液相部、63……補助原
料容器の気相部、64……ガス吹込管、65……
原料補給管、65a,65c……原料補給管の縦
管部、65b……原料補給管の横管部、66……
大気連通用配管、67……補助配管、68〜73
……制御弁。
FIG. 1 is an explanatory diagram schematically showing one embodiment of the raw material replenishing device according to the present invention, and FIG. 2 is an explanatory diagram schematically showing another embodiment of the same. 31...Main raw material container, 61...Auxiliary raw material container,
62... Liquid phase part of the auxiliary raw material container, 63... Gas phase part of the auxiliary raw material container, 64... Gas blowing pipe, 65...
Raw material supply pipes, 65a, 65c...Vertical pipe portion of raw material supply pipe, 65b...Horizontal pipe part of raw material supply pipe, 66...
Atmospheric communication piping, 67...Auxiliary piping, 68-73
...control valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 内部の液体原料を気化してその気化原料を外部
へ取り出す主原料容器内に、原料補給用の配管系
を介して補助原料容器内の液体原料を補給する装
置において、液体原料を収容した密閉型の上記補
助原料容器はガス吹込管、原料補給管、大気連通
用配管、補助配管を備え、上記ガス吹込管は、そ
の管路中に制御弁を有して補助原料容器の気相部
に挿入されており、制御弁を有する両端の縦管部
と、これら両縦管部にわたる横管部とからなる上
記原料補給管は、その一方の縦管部が補助原料容
器内に、その他方の縦管部が主原料容器内にそれ
ぞれ挿入されているとともに、その横管部が主原
料容器側から補助原料容器側に向けて下降する勾
配を有し、上記大気連通用配管は、その管路中に
制御弁を有して補助原料容器の気相部に挿入され
ており、上記補助配管は、その管路中に制御弁を
有してその一端がガス吹込管に、その他端が原料
補給管の最高位部にそれぞれ接続されている原料
補給装置。
A device that replenishes liquid raw materials in an auxiliary raw material container through a piping system for replenishing raw materials into a main raw material container that vaporizes the liquid raw materials inside and takes out the vaporized raw materials to the outside. The auxiliary raw material container is equipped with a gas blowing pipe, a raw material supply pipe, an atmospheric communication pipe, and an auxiliary pipe, and the gas blowing pipe has a control valve in the pipe line and is inserted into the gas phase part of the auxiliary raw material container. The raw material replenishment pipe consists of a vertical pipe section at both ends with a control valve and a horizontal pipe section spanning both vertical pipe sections, with one vertical pipe section inside the auxiliary raw material container and the other vertical pipe section. The pipe portions are inserted into the main raw material containers, and the horizontal pipe portions have a slope that descends from the main raw material container side to the auxiliary raw material container side, and the above-mentioned atmosphere communication pipe is inserted into the main raw material container. The auxiliary pipe has a control valve in the pipe and is inserted into the gas phase part of the auxiliary raw material container, and the auxiliary pipe has a control valve in the pipe, one end of which is connected to the gas blowing pipe, and the other end of which is connected to the raw material supply pipe. Raw material replenishment equipment connected to the highest part of each.
JP4592886U 1986-03-28 1986-03-28 Expired JPH0351313Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4592886U JPH0351313Y2 (en) 1986-03-28 1986-03-28

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4592886U JPH0351313Y2 (en) 1986-03-28 1986-03-28

Publications (2)

Publication Number Publication Date
JPS62157940U JPS62157940U (en) 1987-10-07
JPH0351313Y2 true JPH0351313Y2 (en) 1991-11-01

Family

ID=30865115

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4592886U Expired JPH0351313Y2 (en) 1986-03-28 1986-03-28

Country Status (1)

Country Link
JP (1) JPH0351313Y2 (en)

Also Published As

Publication number Publication date
JPS62157940U (en) 1987-10-07

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