JPH055941Y2 - - Google Patents
Info
- Publication number
- JPH055941Y2 JPH055941Y2 JP17870487U JP17870487U JPH055941Y2 JP H055941 Y2 JPH055941 Y2 JP H055941Y2 JP 17870487 U JP17870487 U JP 17870487U JP 17870487 U JP17870487 U JP 17870487U JP H055941 Y2 JPH055941 Y2 JP H055941Y2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- temperature
- heating plate
- chamber
- flow meter
- 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 - Lifetime
Links
- 239000002994 raw material Substances 0.000 claims description 42
- 238000010438 heat treatment Methods 0.000 claims description 25
- 230000008016 vaporization Effects 0.000 claims description 16
- 238000009834 vaporization Methods 0.000 claims description 15
- 239000007789 gas Substances 0.000 description 9
- 239000007788 liquid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 229910003902 SiCl 4 Inorganic materials 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000013307 optical fiber Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- 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、半導体素子や光フアイバーを製造す
るために使用される液体または固体原料(例えば
SiCl4,GeCl4,WF6,TEOS等)の気化供給を精
密かつ安定に制御するための原料気化供給制御装
置に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention is applicable to liquid or solid raw materials (e.g.
This invention relates to a raw material vaporization and supply control device for precisely and stably controlling the vaporization and supply of SiCl 4 , GeCl 4 , WF 6 , TEOS, etc.).
[従来の技術]
従来、半導体素子や光フアイバーを製造するた
めの原料を気化して供給する方法として、キヤリ
アガスを用いないで、フアン及びフイン付ヒータ
による強制対流を利用した恒温槽内に、原料容
器、質量流量計、それらの間の配管、及び必要な
バルブを収容し、それらを高温に保つて流量制御
を行う方法がある。第3図はその構成を示すもの
で、恒温槽1内に、原料容器2、質量流量計3、
流路の切換えに必要なバルブ4,4,…、並びに
それらを接続する配管5を配設し、それらを高温
に保つためのフイン付ヒータ6の熱をフアン7よ
る強制対流により循環させ、恒温槽内を高温に保
つている。[Prior Art] Conventionally, as a method for vaporizing and supplying raw materials for manufacturing semiconductor devices and optical fibers, the raw materials are stored in a thermostatic chamber using forced convection using a fan and a heater with fins, without using a carrier gas. There is a method of controlling the flow rate by accommodating a container, a mass flow meter, piping between them, and necessary valves and keeping them at a high temperature. Figure 3 shows its configuration, in which a constant temperature bath 1 contains a raw material container 2, a mass flow meter 3,
The valves 4, 4, ... necessary for switching the flow paths and the piping 5 connecting them are arranged, and the heat of the finned heater 6 to keep them at high temperature is circulated by forced convection by the fan 7 to maintain a constant temperature. The inside of the tank is kept at a high temperature.
しかしながら、このような装置により原料の気
化制御を行う場合、次のような問題点があつた。 However, when controlling the vaporization of raw materials using such an apparatus, the following problems occur.
(1) 恒温槽1内の強制対流では、恒温槽内に配管
5及び原料容器2等があるため、風の当り易い
所と当りにくい所ができてしまう。それによつ
て、配管5に温度の低い箇所があると、液体原
料の液化等がおこり、温度の高い部分が質量流
量計3の付近にあれば、流量制御に支障をきた
すおそれがある。(1) In the case of forced convection in the thermostatic chamber 1, since there are piping 5, raw material containers 2, etc. inside the thermostatic chamber, there are areas where the air is easily exposed and areas where it is difficult to reach. As a result, if there is a low-temperature part in the piping 5, liquefaction of the liquid raw material may occur, and if a high-temperature part is near the mass flowmeter 3, there is a risk that flow rate control will be hindered.
また、配管の設計変更のたびに、風の当り具
合が変化するため、温度測定及び調整が必要と
なり、設計コストが高くなる。 Furthermore, each time the design of the piping is changed, the degree of airflow changes, which requires temperature measurement and adjustment, which increases the design cost.
(2) 質量流量計3のガス流路部、バルブのガス流
路部は、SUS316の角材等でできているため、
熱容量が極めて大きく、恒温槽1の強制対流の
みで内部まで均一の温度とするには時間がかか
つた。(2) The gas flow path of the mass flow meter 3 and the gas flow path of the valve are made of SUS316 square material, etc.
The heat capacity was extremely large, and it took a long time to maintain a uniform temperature inside the thermostatic chamber 1 using forced convection alone.
(3) フアン7及びフイン付ヒータ6のスペースや
風通しをよくするためのバルブ等の間のスペー
スが必要であり、装置が大がかりとなる。(3) A space is required between the fan 7 and the heater 6 with fins, and a space between the valves and the like for improving ventilation, making the device large-scale.
[考案が解決しようとする問題点]
上述の原料気化供給装置においては、恒温槽内
の各部が必ずしも高精度に均一な温度である必要
はなく、例えば、原料容器2のように数℃程度の
範囲で温度が低めでよい部分、ガス系のパージラ
イン等のように温度が多少高めで良い部分、質量
流量計3付近や原料の流れる配管5、バルブ4付
近のように、厳密に一定温度でなければならない
部分に分けることができる。[Problems to be solved by the invention] In the above-mentioned raw material vaporization and supply device, it is not necessary that each part in the thermostatic chamber has a uniform temperature with high precision. There are areas where the temperature can be lower in the range, areas where the temperature can be slightly higher, such as gas purge lines, areas where the temperature can be kept at a strictly constant temperature, such as areas near the mass flow meter 3, pipes 5 and valves 4 where raw materials flow. It can be divided into the necessary parts.
本考案は、このような点を考慮し、簡単な手段
によつて、上述の従来の問題点を解消しながら、
各部を適切な温度範囲に制御できるようにした原
料気化供給制御装置を得ようとするものである。 Taking these points into consideration, the present invention solves the above-mentioned conventional problems by simple means, and
The present invention aims to provide a raw material vaporization and supply control device that can control each part within an appropriate temperature range.
[問題点を解決するための手段]
上記目的を達成するため、本考案においては、
原料容器に収容した原料を加熱気化し、気化した
原料を質量流量計及びバルブ、並びにそれらを接
続する原料ガス供給配管を介して送出するように
した原料気化供給制御装置において、恒温槽内を
ヒータ内蔵のヒーテイングプレートにより上下の
室に分割し、上室内において、温度制御されるヒ
ーテイングプレート上に質量流量計及びバルブの
通路形成部材を密着して取付けると共に、それら
を接続する原料ガス供給配管を所要の高さに配設
し、下室内に、内部の原料温度を一定に保持する
ように制御された原料容器を配設する、という技
術的手段を採用している。[Means for solving the problem] In order to achieve the above purpose, in the present invention,
In a raw material vaporization and supply control device that heats and vaporizes the raw material contained in a raw material container and sends the vaporized raw material through a mass flow meter, a valve, and a raw material gas supply piping that connects them, the inside of the thermostatic chamber is heated and vaporized. The upper chamber is divided into upper and lower chambers by a built-in heating plate, and in the upper chamber, the mass flow meter and valve passage forming member are closely attached to the temperature-controlled heating plate, and the source gas supply piping connects them. A technical measure is adopted in which a container is placed at a desired height and a raw material container is placed in the lower chamber, which is controlled to maintain a constant temperature of the raw material inside.
[作用]
ヒーテイングプレート上に密着させた質量流量
計やバルブの通路形成部材は、熱容量が大きい
が、ヒーテイングプレートからの直接的な熱伝導
により加熱されるので、一定温度にするための時
間が短縮される。また、ヒーテイングプレートに
より区画した上室に質量流量計、バルブ及びそれ
らを接続する配管を適切に配設しているので、簡
単な手段によつて、各部が適切な温度範囲に制御
される。[Function] The passage forming members of mass flowmeters and valves that are placed in close contact with the heating plate have a large heat capacity, but because they are heated by direct heat conduction from the heating plate, it takes a long time to reach a constant temperature. is shortened. Furthermore, since the mass flow meter, valves, and piping connecting them are appropriately arranged in the upper chamber partitioned by the heating plate, each part can be controlled within an appropriate temperature range by simple means.
[実施例]
第1図及び第2図は本考案に係る原料気化供給
制御装置の実施例を示している。[Embodiment] FIGS. 1 and 2 show an embodiment of the raw material vaporization and supply control device according to the present invention.
この原料気化供給制御装置において、断熱材の
壁によつて囲まれた恒温槽11内は、ヒータ内蔵
のヒーテイングプレート12を水平に配置して、
その内部を上室13と下室14に分割している。
このヒーテイングプレート12は、恒温槽11内
を上下に気密に仕切るものではなく、上室13と
下室14との間に大きな空気の流れが生じないよ
うにする程度のものである。 In this raw material vaporization supply control device, a heating plate 12 with a built-in heater is arranged horizontally in a constant temperature chamber 11 surrounded by a wall of heat insulating material.
The interior is divided into an upper chamber 13 and a lower chamber 14.
The heating plate 12 is not intended to airtightly partition the interior of the thermostatic chamber 11 into upper and lower sections, but rather to prevent a large air flow from occurring between the upper chamber 13 and the lower chamber 14.
上記ヒーテイングプレート12は、下層を断熱
層15とし、その上層にステンレス鋼やアルミニ
ウム等のような熱伝導率の良い材料からなる伝熱
板16を重設し、さらにその上層の必要部分に薄
板状のヒータ17を密着させたものである。 The heating plate 12 has a heat insulating layer 15 as the lower layer, a heat transfer plate 16 made of a material with good thermal conductivity such as stainless steel or aluminum on the upper layer, and a thin plate on the necessary parts of the upper layer. A heater 17 of a shape is placed in close contact with the heater 17.
ヒーテイングプレート12により区画された上
室13内には、質量流量計20、流路の切換えに
必要なバルブ21,21,…、並びにそれらを接
続する原料ガス供給配管22を配設し、質量流量
計20及びバルブ21は、内部に流体の通路が形
成された熱容量の大きい通路形成部材20a,2
1aを熱伝導により直接加熱するため、ヒーテイ
ングプレート12上に密着して取付けている。図
示した実施例では、質量流量計20、バルブ21
をヒータ17上に設置しているが、ヒーテイング
プレート12上に設けた伝熱板16によりほぼ全
面に良好な伝熱が行われるので、必ずしもそれら
をヒータ17上に設ける必要はない。 In the upper chamber 13 partitioned by the heating plate 12, a mass flow meter 20, valves 21, 21, etc. necessary for switching the flow paths, and raw material gas supply piping 22 connecting these are arranged. The flow meter 20 and the valve 21 are made of passage forming members 20a, 2 having a large heat capacity and having a fluid passage formed therein.
In order to directly heat 1a by thermal conduction, it is attached in close contact with the heating plate 12. In the illustrated embodiment, a mass flow meter 20, a valve 21
are installed on the heater 17, but since the heat transfer plate 16 provided on the heating plate 12 ensures good heat transfer over almost the entire surface, it is not necessary to provide them on the heater 17.
上室13の温度制御は、厳密な温度制御を必要
とする質量流量計20の通路形成部材20a,2
1aに温度センサ23を取付け、この温度センサ
23の出力に応じてヒータ17による加熱を調整
することにより行つている。ヒーテイングプレー
ト12上のバルブ21及び質量流量計20等の間
を接続している原料ガス供給配管22は、この上
室13内において温度制御されるが、その配管2
2中で同一の温度に保持すべき部分をヒーテイン
グプレート12から同じ高さに位置させ、それに
よつて配管温度を一定に保つようにしている。 The temperature of the upper chamber 13 is controlled by passage forming members 20a and 2 of the mass flowmeter 20, which require strict temperature control.
This is achieved by attaching a temperature sensor 23 to 1a and adjusting the heating by the heater 17 according to the output of this temperature sensor 23. The temperature of the source gas supply pipe 22 connecting between the valve 21 on the heating plate 12 and the mass flow meter 20 etc. is controlled in the upper chamber 13.
The parts of the pipes 2 to be maintained at the same temperature are located at the same height from the heating plate 12, thereby keeping the pipe temperature constant.
原料ガス供給配管は、ヒーテイングプレート1
2からの距離によつて温度傾斜をつけることがで
き、例えば、パージライン等の原料の流れない配
管や、温度を他の配管と異なる温度に設定したい
配管や、ヒーテイングプレート12からの距離を
変化させることにより、配管温度に適宜傾斜をつ
けることも可能である。 The raw material gas supply piping is connected to heating plate 1.
For example, it is possible to set a temperature gradient depending on the distance from the heating plate 12, for example, for piping where raw materials do not flow such as a purge line, for piping where you want to set the temperature to be different from other piping, or for piping where you want to set the temperature to be different from other piping, or by changing the distance from the heating plate 12. By changing the temperature, it is also possible to appropriately incline the pipe temperature.
上記上室13は、質量流量計20及びバルブ2
1を主体として設置し、その室内の温度を制御す
るので、上室13自体の高さを、それらの設置に
必要な高さで可及的に低くするのが望ましく、一
般的にその高さは20cm以下に設定される。このよ
うに、上室13の高さを可及的に低くすること
は、上室13に強制対流用のフイン付きヒータ及
びフアン等を設置することなく、配管温度を一定
にするために、極めて有効である。 The upper chamber 13 includes a mass flowmeter 20 and a valve 2.
Since the upper chamber 13 is installed as the main body and the temperature inside the room is controlled, it is desirable to make the height of the upper chamber 13 itself as low as possible by the height necessary for the installation, and generally the height is set to 20cm or less. In this way, it is extremely important to make the height of the upper chamber 13 as low as possible in order to keep the pipe temperature constant without installing a finned heater or fan for forced convection in the upper chamber 13. It is valid.
また、上記実施例においては、上室13を下室
14より高温に保持するため、ヒーテイングプレ
ート12の下層に断熱層15を配しているが、両
室の温度を如何に設定するかにより、この断熱層
15を省略することもできる。 Further, in the above embodiment, in order to maintain the upper chamber 13 at a higher temperature than the lower chamber 14, a heat insulating layer 15 is disposed below the heating plate 12, but depending on how the temperature of both chambers is set, , this heat insulating layer 15 can also be omitted.
一方、上記下室14には原料容器24を配設し
ている。原料容器24内は原料の気化熱により温
度が下がるため、別に温度計25及びヒータ26
を付け、それらにより原料温度を一定にするため
の制御を行つている。 On the other hand, a raw material container 24 is disposed in the lower chamber 14. Since the temperature inside the raw material container 24 drops due to the heat of vaporization of the raw material, a thermometer 25 and a heater 26 are separately installed.
are used to control the raw material temperature to a constant level.
なお、ヒーテイングプレート12を複数段と
し、各段により区画される室を別々に温度調節す
ることも可能である。 Note that it is also possible to have multiple stages of the heating plate 12 and to separately adjust the temperature of the chambers partitioned by each stage.
上記構成を有する原料気化供給装置において
は、ヒーテイングプレート12上に質量流量計2
0やバルブ21の通路形成部材20a,21aを
密着させ、直接熱伝導により加熱するようにして
いるので、熱容量の大きな通路形成部材を一定温
度にするための時間が短縮される。 In the raw material vaporization supply device having the above configuration, a mass flowmeter 2 is mounted on the heating plate 12.
Since the passage forming members 20a and 21a of the valve 21 and the valve 21 are brought into close contact with each other and heated by direct heat conduction, the time required to bring the passage forming members having a large heat capacity to a constant temperature is shortened.
また、質量流量計20の通路形成部材20a,
21aに温度センサ23を取付けて温度制御を行
うようにしているので、特に質量流量計20を高
精度に温度調節でき、その質量流量計20と同じ
上室13に設けたバルブ21や配管22も比較的
精度よく、しかもそれらに適した温度調節を行う
ことが可能である。 Moreover, the passage forming member 20a of the mass flowmeter 20,
Since temperature control is performed by attaching a temperature sensor 23 to 21a, the temperature of the mass flowmeter 20 can be adjusted with high precision, and the valve 21 and piping 22 installed in the same upper chamber 13 as the mass flowmeter 20 can also be adjusted. It is possible to adjust the temperature with relative accuracy and in a manner suitable for these conditions.
さらに、この装置の設計変更を行い、あるいは
新しく設計を行う場合にも、各要素を上室13の
ヒーテイングプレート上及び下室14に並べ、配
管22をヒーテイングプレート12から等距離に
配置するだけで、所期の温度制御を行うことが可
能なため、フアンを用いる場合のように、予め風
の当たり具合により変化する温度の測定等を行う
必要がなくなり、そのため設計コストがかからな
い。 Furthermore, when changing the design of this device or creating a new design, each element should be arranged on the heating plate in the upper chamber 13 and on the lower chamber 14, and the piping 22 should be arranged at an equal distance from the heating plate 12. Since it is possible to perform the desired temperature control with just the fan, there is no need to measure the temperature that changes depending on the wind blowing condition in advance, unlike when using a fan, and therefore the design cost is reduced.
[考案の効果]
以上に詳述したように、本考案の原料気化供給
制御装置によれば、恒温槽内の各部が必ずしも高
精度に均一な温度になる必要がなく、数℃程度の
範囲で温度が低めまたは高めで良い部分、厳密に
一定温度でなければならない部分等が分かれるこ
とを考慮し、設計コストのかからない簡単な手段
によつて、各部を迅速に適切な温度範囲に制御す
ることができ、また従来の装置のように強制対流
用のフイン付ヒータやフアン等を設ける必要がな
いため、それだけ恒温槽の容積を小さくすること
ができる。[Effects of the invention] As detailed above, according to the raw material vaporization supply control device of the invention, it is not necessary that each part in the thermostatic chamber has a uniform temperature with high precision, but within a range of several degrees Celsius. Considering that there are parts that require a lower or higher temperature, and parts that require a strictly constant temperature, it is possible to quickly control each part to an appropriate temperature range using simple means that do not require design costs. Moreover, unlike conventional devices, there is no need to provide a finned heater or fan for forced convection, so the volume of the thermostatic chamber can be reduced accordingly.
第1図は本考案に係る原料気化供給制御装置の
縦断面図、第2図は同水平断面図、第3図は従来
の原料気化供給制御装置の縦断面図である。
11……恒温槽、12……ヒーテイングプレー
ト、13……上室、14……下室、17,26…
…ヒータ、20……質量流量計、20a,21a
……通路形成部材、21……バルブ、22……原
料ガス供給配管、24……原料容器。
FIG. 1 is a longitudinal sectional view of a raw material vaporization and supply control device according to the present invention, FIG. 2 is a horizontal sectional view thereof, and FIG. 3 is a longitudinal sectional view of a conventional raw material vaporization and supply control device. 11... Constant temperature chamber, 12... Heating plate, 13... Upper chamber, 14... Lower chamber, 17, 26...
...Heater, 20...Mass flow meter, 20a, 21a
... Passage forming member, 21 ... Valve, 22 ... Raw material gas supply piping, 24 ... Raw material container.
Claims (1)
た原料を質量流量計及びバルブ、並びにそれらを
接続する原料ガス供給配管を介して送出するよう
にした原料気化供給制御装置において、 恒温槽内をヒータ内蔵のヒーテイングプレート
により上下の室に分割し、 上室内において、温度制御されるヒーテイング
プレート上に質量流量計及びバルブの通路形成部
材を密着して取付けると共に、それらを接続する
原料ガス供給配管を所要の高さに配設し、 下室内に、内部の原料温度を一定に保持するよ
うに制御された原料容器を配設した、 ことを特徴とする原料気化供給制御装置。[Claim for Utility Model Registration] Raw material vaporization and supply control that heats and vaporizes the raw material contained in a raw material container and sends the vaporized raw material through a mass flow meter, a valve, and a raw material gas supply pipe that connects them. In the device, the inside of the constant temperature chamber is divided into upper and lower chambers by a heating plate with a built-in heater, and in the upper chamber, the mass flow meter and the passage forming member of the valve are closely mounted on the heating plate whose temperature is controlled. A raw material vaporization system characterized in that a raw material gas supply pipe connecting these is arranged at a required height, and a raw material container that is controlled to keep the internal raw material temperature constant is arranged in the lower chamber. Supply control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17870487U JPH055941Y2 (en) | 1987-11-24 | 1987-11-24 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17870487U JPH055941Y2 (en) | 1987-11-24 | 1987-11-24 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0183432U JPH0183432U (en) | 1989-06-02 |
| JPH055941Y2 true JPH055941Y2 (en) | 1993-02-16 |
Family
ID=31470311
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17870487U Expired - Lifetime JPH055941Y2 (en) | 1987-11-24 | 1987-11-24 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH055941Y2 (en) |
-
1987
- 1987-11-24 JP JP17870487U patent/JPH055941Y2/ja not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0183432U (en) | 1989-06-02 |
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