JPS6310310B2 - - Google Patents
Info
- Publication number
- JPS6310310B2 JPS6310310B2 JP8572083A JP8572083A JPS6310310B2 JP S6310310 B2 JPS6310310 B2 JP S6310310B2 JP 8572083 A JP8572083 A JP 8572083A JP 8572083 A JP8572083 A JP 8572083A JP S6310310 B2 JPS6310310 B2 JP S6310310B2
- Authority
- JP
- Japan
- Prior art keywords
- helium
- helium refrigerator
- refrigerator
- thin film
- shroud
- 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
- 239000001307 helium Substances 0.000 claims description 61
- 229910052734 helium Inorganic materials 0.000 claims description 61
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 61
- 239000010409 thin film Substances 0.000 claims description 33
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 29
- 239000007789 gas Substances 0.000 claims description 23
- 239000000463 material Substances 0.000 claims description 14
- 239000004065 semiconductor Substances 0.000 claims description 14
- 239000000758 substrate Substances 0.000 claims description 12
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 7
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 12
- 238000002360 preparation method Methods 0.000 description 12
- 239000007788 liquid Substances 0.000 description 11
- 238000009835 boiling Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000001105 regulatory effect Effects 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000001451 molecular beam epitaxy Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B37/00—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00
- F04B37/06—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for evacuating by thermal means
- F04B37/08—Pumps having pertinent characteristics not provided for in, or of interest apart from, groups F04B25/00 - F04B35/00 for evacuating by thermal means by condensing or freezing, e.g. cryogenic pumps
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
- Physical Deposition Of Substances That Are Components Of Semiconductor Devices (AREA)
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明はヘリウム冷凍機を応用したクライオポ
ンプ排気システムに係り、特に半導体薄膜生成装
置に適用して好適な真空排気装置に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a cryopump exhaust system using a helium refrigerator, and particularly to a vacuum exhaust system suitable for application to a semiconductor thin film production apparatus.
従来、分子線エピタキシに代表される半導体薄
膜生成装置の構成ならびに真空排気装置は、第1
図に示すようになつているのが一般的である。
Conventionally, the configuration and vacuum evacuation equipment of semiconductor thin film production equipment, typified by molecular beam epitaxy, are
It is generally arranged as shown in the figure.
1は試料交換室、2は真空バルブ、3はターボ
分子ポンプ等に代表される高真空ポンプ、4はリ
ークバルブ、5は高真空ポンプ3の背圧排気に用
いられるロータリーポンプ、6は高真空チヤンバ
である試料準備・分析室、7は同じく高真空チヤ
ンバである薄膜成長室、8,9,10,11はゲ
ートバルブ、12,13はスパツタイオンポンプ
やクライオポンプに代表される油蒸気の逆拡散が
ないクリーンな超高真空ポンプ、14は試料基板
ホルダー、15は試料基板の平行移動や回転を行
うマニピユレータ、16は試料基板上に薄膜の素
材を供給する素材供給源(分子線エピタキシの場
合は分子線源)、17,18は薄膜成長室7の中
に浮遊するガス分子を凝縮吸着させて真空排気作
用を行うための液体窒素シユラウドである。 1 is a sample exchange chamber, 2 is a vacuum valve, 3 is a high vacuum pump such as a turbo molecular pump, 4 is a leak valve, 5 is a rotary pump used for exhausting back pressure of the high vacuum pump 3, and 6 is a high vacuum The sample preparation/analysis room is a chamber; 7 is a thin film growth chamber which is also a high vacuum chamber; 8, 9, 10, and 11 are gate valves; A clean ultra-high vacuum pump with no back diffusion, 14 a sample substrate holder, 15 a manipulator for parallel translation and rotation of the sample substrate, and 16 a material supply source (for molecular beam epitaxy) that supplies a thin film material onto the sample substrate. 17 and 18 are liquid nitrogen shrouds for condensing and adsorbing gas molecules floating in the thin film growth chamber 7 and performing a vacuum evacuation action.
次に、この装置の作用について説明すると、試
料交換室1、試料準備・分析室6ならびに薄膜成
長室7をすべて気密にし、試料交換室1に試料を
入れた後ゲートバルブ9,11を閉にゲートバル
ブ8,10を閉にし、真空バルブ2を開きリーク
バルブ4を閉じた状態でロータリポンプ5を駆動
する。そして、試料交換室1をはじめとした真空
排気空間が0.1Torr以下の圧力になつたところで
高真空ポンプ3を作動させる。真空排気空間の圧
力がさらに低下してきたところ(一般には
10-4Torr以下)でゲートバルブ9,11を開き、
ゲートバルブ8を閉じてクリーンな超高真空ポン
プ12,13を作動させる。 Next, to explain the operation of this device, the sample exchange chamber 1, sample preparation/analysis chamber 6, and thin film growth chamber 7 are all made airtight, and after the sample is put into the sample exchange chamber 1, the gate valves 9 and 11 are closed. The rotary pump 5 is driven with the gate valves 8 and 10 closed, the vacuum valve 2 opened, and the leak valve 4 closed. Then, when the vacuum evacuation space including the sample exchange chamber 1 reaches a pressure of 0.1 Torr or less, the high vacuum pump 3 is activated. When the pressure in the vacuum evacuation space has further decreased (generally
10 -4 Torr or less), open gate valves 9 and 11,
The gate valve 8 is closed and the clean ultra-high vacuum pumps 12 and 13 are operated.
試料準備・分析室6、薄膜成長室7の圧力が十
分低下し、所期の目標圧力まで低下したらゲート
バルブ10を閉じてゲートバルブ8を開き、試料
交換室1の中の試料を搬送装置(図示せず)で試
料準備・分析室6の中に移動させる。次いで、ゲ
ートバルブ8を閉じてゲートバルブ10を開き、
試料を薄膜成長室7の中の試料基板ホルダー14
の上にセツトすると同時にゲートバルブ10を閉
じる。その間、超高真空ポンプ12,13は作動
を継続している。 When the pressure in the sample preparation/analysis chamber 6 and thin film growth chamber 7 is sufficiently reduced to the desired target pressure, the gate valve 10 is closed and the gate valve 8 is opened, and the sample in the sample exchange chamber 1 is transferred to the transfer device ( (not shown) into the sample preparation/analysis room 6. Next, close the gate valve 8 and open the gate valve 10,
The sample is placed in the sample substrate holder 14 in the thin film growth chamber 7.
At the same time, the gate valve 10 is closed. Meanwhile, the ultra-high vacuum pumps 12 and 13 continue to operate.
薄膜成長室7の圧力が目標値まで低下したら、
素材供給源(分子線源)16から試料基板上に半
導体の素材をとばして薄膜を生成する。 When the pressure in the thin film growth chamber 7 drops to the target value,
A semiconductor material is blown onto a sample substrate from a material supply source (molecular beam source) 16 to form a thin film.
一方、薄膜成長室7において素材供給時に発生
する不銃物は液体窒素シユラウド17,18の上
に凝縮吸着され、薄膜試料中に欠陥が生ずるのを
防ぐ。薄膜成長室7で試料基板上に薄膜を生成し
た後、試料は試料準備・分析室6で所定のものが
得られたかどうかチエツクされ、試料交換室1を
経由して外に搬出される。 On the other hand, non-gun materials generated during material supply in the thin film growth chamber 7 are condensed and adsorbed onto the liquid nitrogen shrouds 17 and 18, thereby preventing defects from occurring in the thin film sample. After a thin film is formed on the sample substrate in the thin film growth chamber 7, the sample is checked in the sample preparation/analysis chamber 6 to see if the desired one has been obtained, and then transported outside via the sample exchange chamber 1.
このような従来方式の半導体薄膜生成装置の真
空排気装置においては、次のような欠点があつ
た。 The vacuum evacuation device of such a conventional semiconductor thin film production apparatus has the following drawbacks.
すなわち、液体窒素シユラウド17,18の冷
却源である液体窒素は、従来外部に設置した液体
窒素容器から供給し蒸発したガスは大気中に放出
する、いわゆる使い捨てであつた。したがつて、
液体窒素代がかさむ上液体窒素の定期的な補給が
煩わしいという欠点があつた。 That is, the liquid nitrogen that is the cooling source for the liquid nitrogen shrouds 17 and 18 has conventionally been supplied from a liquid nitrogen container installed outside, and the evaporated gas is discharged into the atmosphere, so-called disposable. Therefore,
The drawbacks were that the cost of liquid nitrogen was high and that periodic replenishment of liquid nitrogen was troublesome.
また、薄膜成長室7と試料準備・分析室6にお
のおの別々に超高真空ポンプ12,13を設置し
ているのは不経済であつた。 Furthermore, it is uneconomical to separately install ultra-high vacuum pumps 12 and 13 in the thin film growth chamber 7 and the sample preparation/analysis chamber 6.
本発明の目的は、上記のごとき従来の半導体薄
膜生成装置の真空排気装置における欠点を解消
し、経済的で煩わしさのない真空排気装置を提供
することにある。
An object of the present invention is to eliminate the drawbacks of the conventional vacuum evacuation apparatus for semiconductor thin film production apparatuses as described above, and to provide an economical and trouble-free evacuation apparatus.
本発明の特徴は、液体窒素シユラウドに代えて
ヘリウム冷凍機によつて冷却されるシユラウドを
用い、薄膜成長室や試料準備・分析室の超高真空
ポンプにもヘリウム冷凍機によつて冷却されるク
ライオポンプを用い、こら複数台のヘリウム冷凍
機を1台のヘリウム圧縮機に連結して運転するよ
うにしたことにある。
A feature of the present invention is that a shroud cooled by a helium refrigerator is used instead of a liquid nitrogen shroud, and ultra-high vacuum pumps in the thin film growth chamber and sample preparation/analysis room are also cooled by the helium refrigerator. Using a cryopump, multiple helium refrigerators are connected to one helium compressor for operation.
以下、本発明の一実施例を第2図によつて説明
する。第1図と同一の構成部品は同一符号で示
す。まず構成についてみると、21,22は2段
式のヘリウム冷凍機28,29を適用したクライ
オポンプ、24a,24bは1段式ヘリウム冷凍
機23によつて冷却されるシユラウドで、それぞ
れ素材供給源(分子線源)16、試料基板ホルダ
ー14を囲むように配置されている。25a,2
5b,25cはヘリウム圧縮機27からヘリウム
冷凍機28,29,23に高圧ヘリウムガスを供
給するためのガス供給管、26a,26b,26
cはヘリウム冷凍機28,29,23からヘリウ
ム圧縮機27に低圧ヘリウムガスを循環させるた
めのガス戻し管である。
An embodiment of the present invention will be described below with reference to FIG. Components that are the same as in FIG. 1 are designated by the same reference numerals. First, looking at the configuration, 21 and 22 are cryopumps to which two-stage helium refrigerators 28 and 29 are applied, and 24a and 24b are shrouds cooled by a single-stage helium refrigerator 23, respectively, which are the material supply sources. (Molecular beam source) 16 is arranged so as to surround the sample substrate holder 14. 25a, 2
5b, 25c are gas supply pipes for supplying high pressure helium gas from the helium compressor 27 to the helium refrigerators 28, 29, 23; 26a, 26b, 26;
C is a gas return pipe for circulating low-pressure helium gas from the helium refrigerators 28, 29, and 23 to the helium compressor 27.
次にこの装置の作用について説明すると、高真
空ポンプ3を作動させて真空排気空間である試料
交換室1、試料準備・分析室6ならびに薄膜成長
室7を10-4Torr程度にするまでは、従来と同一
手順で行う。その後、ゲートバルブ8を閉じゲー
トバルブ9,11を開にし、ヘリウム圧縮機2
7、ヘリウム冷凍機23,28,29を運転開始
する。 Next, to explain the operation of this device, until the high vacuum pump 3 is activated and the vacuum evacuation spaces such as the sample exchange chamber 1, sample preparation/analysis chamber 6, and thin film growth chamber 7 are brought to about 10 -4 Torr, Follow the same procedure as before. After that, the gate valve 8 is closed, the gate valves 9 and 11 are opened, and the helium compressor 2
7. Start operating the helium refrigerators 23, 28, and 29.
ヘリウム冷凍機23,28,29の温度が低下
するにしたがつてクライオポンプ21,22は超
高真空ポンプとして作用しはじめる。また、シユ
ラウド24a,24bも冷却されて真空ポンプと
して作用しはじめる。 As the temperature of the helium refrigerators 23, 28, 29 decreases, the cryopumps 21, 22 begin to function as ultra-high vacuum pumps. Furthermore, the shrouds 24a and 24b are also cooled and begin to function as a vacuum pump.
一方、その間も高真空ポンプ3を作動させてお
き、試料交換室1での圧力が十分に低くなつたと
き(例えば10-8Torr程度まで下つたとき)ゲー
トバルブ8,10を開き、試料を試料交換室1か
ら搬送装置(図示せず)によつて試料準備・分析
室6を経て薄膜成長室7の中の試料基板ホルダー
14の上に移動させる。 Meanwhile, the high vacuum pump 3 is kept operating during this time, and when the pressure in the sample exchange chamber 1 becomes low enough (for example, down to about 10 -8 Torr), the gate valves 8 and 10 are opened and the sample is removed. The sample is transferred from the sample exchange chamber 1 to the sample substrate holder 14 in the thin film growth chamber 7 via the sample preparation/analysis chamber 6 by a transport device (not shown).
次いで、ゲートバルブ8,10を閉じ、薄膜成
長室7の圧力が初期の目標まで低下したところで
素材供給源(分子線源)16から試料基板上に半
導体の素材をとばして薄膜を生成する。そして、
薄膜成長室7において素材をとばすときに発生す
る不純物等の浮遊物はヘリウム冷凍機23によつ
て冷却されたシユラウド24a,24bに凝縮吸
着され、これらの浮遊不純物が薄膜試料中に混入
して欠陥になるのを防ぐ作用を行う。 Next, the gate valves 8 and 10 are closed, and when the pressure in the thin film growth chamber 7 has decreased to the initial target, the semiconductor material is blown onto the sample substrate from the material supply source (molecular beam source) 16 to form a thin film. and,
Floating substances such as impurities generated when the material is blown away in the thin film growth chamber 7 are condensed and adsorbed on the shrouds 24a and 24b cooled by the helium refrigerator 23, and these floating impurities mix into the thin film sample and cause defects. It acts to prevent this from happening.
本実施例に用いられるヘリウム冷凍機のうちク
ライオポンプ21,22に用いられるヘリウム冷
凍機28,29が2段式になつているのは、超高
真空ポンプとして機能するには十分な低温を得る
必要があるためであり、現状製品における2段目
の低温端は15K程度になる。 Among the helium refrigerators used in this embodiment, the helium refrigerators 28 and 29 used in the cryopumps 21 and 22 are of a two-stage type because they obtain a low temperature sufficient to function as an ultra-high vacuum pump. This is because it is necessary, and the low temperature end of the second stage in the current product is around 15K.
ここで、現状クライオンポンプの概要を第3図
によつて説明すると、第1段シリンダ31の低温
端につけた第1段パネル34は大体50〜70Kとな
り、主に空気中の水分や炭酸ガス等沸点の高いガ
スを凝縮吸着し、第2段シリンダ32の低温端に
つけた第2段パネル36は大体15Kになつて酸
素、窒素、アルゴン等の低沸点ガスを凝縮吸着す
る。さらに沸点の低い水素やヘリウムガス等は第
2段パネル36の内面に貼付けた吸着剤37(例
えば活性炭やモレキユラシーブ等)によつて吸着
する。 Here, an overview of the current Kryon pump will be explained with reference to Fig. 3.The first stage panel 34 attached to the low temperature end of the first stage cylinder 31 has a temperature of about 50 to 70K, and is mainly used for moisture and carbon dioxide gas in the air. The second stage panel 36 attached to the low temperature end of the second stage cylinder 32 condenses and adsorbs gases with a high boiling point, and the temperature reaches approximately 15K, and condenses and adsorbs low boiling point gases such as oxygen, nitrogen, and argon. Further, hydrogen, helium gas, etc. having a low boiling point are adsorbed by an adsorbent 37 (for example, activated carbon, molecular sieve, etc.) attached to the inner surface of the second stage panel 36.
特に、超高真空ポンプとしての性能を左右する
のはこの第2段パネル36の温度をいかに低温に
できるかによつて決まるので、少くとも2段式ヘ
リウム冷凍機が要求されるものである。 In particular, since the performance of the ultra-high vacuum pump is determined by how low the temperature of the second stage panel 36 can be made, at least a two-stage helium refrigerator is required.
シエブロン35は、沸点の高いガスが直接低温
の第2段パネル36に凝縮吸着されることによつ
て第2段パネル36の低沸点ガス吸着能力が低下
するのを防止する機能を持つている。 The Chevron 35 has a function of preventing the low boiling point gas adsorption ability of the second stage panel 36 from being reduced due to direct condensation and adsorption of a high boiling point gas on the low temperature second stage panel 36.
一方、シユラウド24a,24bの冷却に用い
られるヘリウム冷凍機23が1段式になつている
のは、シユラウド24a,24bでは比較的沸点
の高い半導体素材のガスを凝縮吸着するのがその
主な役目であるからさほど低温にする必要はな
く、したがつて1段式でよいわけである。 On the other hand, the helium refrigerator 23 used for cooling the shrouds 24a and 24b is of a single-stage type because its main role in the shrouds 24a and 24b is to condense and adsorb the gas of the semiconductor material, which has a relatively high boiling point. Therefore, there is no need to make the temperature very low, and therefore a one-stage type is sufficient.
本実施例によれば、シユラウド24a,24b
の冷却を1段式ヘリウム冷凍機23で行うことが
できるので別に液体窒素を必要とせず、ランニン
グコストが安くなる上液体窒素の補給作業という
煩わしさもなくなるという効果がある。 According to this embodiment, the shrouds 24a, 24b
can be cooled by the single-stage helium refrigerator 23, so there is no need for liquid nitrogen, which has the effect of reducing running costs and eliminating the hassle of replenishing liquid nitrogen.
さらに、薄膜成長室7、試料準備・分析室6の
超高真空ポンプとしてクライオポンプ28,29
を用い、クライオポンプの2段式ヘリウム冷凍機
21,22と上記シユラウド用1段式ヘリウム冷
凍機23へのヘリウムガス供給を1台のヘリウム
圧縮機27で行うことができるので、真空排気装
置として構成が簡単になり経済的であるという効
果もある。 Furthermore, cryopumps 28 and 29 are used as ultra-high vacuum pumps for the thin film growth chamber 7 and the sample preparation/analysis chamber 6.
By using a single helium compressor 27, helium gas can be supplied to the two-stage helium refrigerators 21 and 22 of the cryopump and the single-stage helium refrigerator 23 for the shroud, so it can be used as a vacuum evacuation device. Another advantage is that the configuration is simple and economical.
第4図は本発明の他の実施例を示す図であり、
ヘリウム圧縮機27に接続された複数台のヘリウ
ム冷凍機へのガスヘリウム供給量を各ヘリウム冷
凍機の要求に応じてコントロールできるようにし
たものである。 FIG. 4 is a diagram showing another embodiment of the present invention,
The amount of gas helium supplied to a plurality of helium refrigerators connected to the helium compressor 27 can be controlled according to the requirements of each helium refrigerator.
すなわち、ヘリウム冷凍機28,29,23へ
のガス供給管25a,25b,25cにガス流量
調整弁41a,41b,41cを備え、試料準
備・分析室6の圧力を下げたいときには調整弁4
1aを開放して41b,41cを絞り加減にし、
また、薄膜生長室7の圧力を下げたいときには調
整弁41bを開放して41a,41cを絞り気味
にする。さらに、シユラウド24a,24bの機
能を向上させたいときには調整弁41cを開放し
て41a,41bを絞り気味にする。 That is, the gas supply pipes 25a, 25b, 25c to the helium refrigerators 28, 29, 23 are equipped with gas flow rate adjustment valves 41a, 41b, 41c, and when it is desired to lower the pressure in the sample preparation/analysis chamber 6, the adjustment valve 4 is provided.
Open 1a, adjust 41b and 41c,
Further, when it is desired to lower the pressure in the thin film growth chamber 7, the regulating valve 41b is opened and the valves 41a and 41c are slightly throttled. Further, when it is desired to improve the functions of the shrouds 24a and 24b, the regulating valve 41c is opened to slightly throttle the shrouds 41a and 41b.
本実施例によれば、複数台のヘリウム冷凍機に
ガスを供給する際に必要に応じて各ヘリウム冷凍
機への供給量を調整することができるので、相対
的にヘリウム圧縮機は小容量ですみ経済的になる
という効果がある。 According to this embodiment, when supplying gas to multiple helium refrigerators, the amount of gas supplied to each helium refrigerator can be adjusted as necessary, so the helium compressor has a relatively small capacity. This has the effect of making it more economical.
本実施例の変形例として、供給管25a,25
b,25cに調整弁を備える代りにガス戻し管2
6a,26b,26cに調整弁を備えても同様な
効果が得られる。また、ヘリウム冷凍機28,2
9,23の往復周波数を支配しているモータ(図
示せず)の回転数を制御してもよい。 As a modification of this embodiment, supply pipes 25a, 25
Gas return pipe 2 instead of providing adjustment valves in b and 25c
A similar effect can be obtained by providing regulating valves 6a, 26b, and 26c. In addition, helium refrigerator 28,2
The rotational speed of a motor (not shown) controlling the reciprocating frequencies of 9 and 23 may be controlled.
第5図は本発明のさらに別の実施例で、シユラ
ウド24a,24bとヘリウム冷凍機23を直接
熱的に接続して冷却する代りに液体窒素でシユラ
ウド24a,24bを冷却し、蒸発した窒素ガス
をヘリウム冷凍機23で再液化させるものであ
る。 FIG. 5 shows still another embodiment of the present invention, in which instead of cooling the shrouds 24a, 24b and the helium refrigerator 23 by directly thermally connecting them, the shrouds 24a, 24b are cooled with liquid nitrogen, and the evaporated nitrogen gas is cooled. is reliquefied using a helium refrigerator 23.
この場合は、蒸発した窒素ガスを上方のガス貯
蔵室42に導き、該貯蔵室42にヘリウム冷凍機
23の低温端を熱的に接触させて冷却することに
より、ここで液化してシユラウド24a,24b
に循環するのでシユラウドが大きくなつてもシユ
ラウドの温度はほぼ均一に保持でき、しかもヘリ
ウム冷凍機23との相対的な位置に制約を受けな
いですむという効果がある。もちろん、この場合
はシユラウド冷却の窒素ガスがヘリウム冷凍機で
再液化されるので、ランニングコストは増大する
ことはない。 In this case, the evaporated nitrogen gas is guided into the upper gas storage chamber 42 and cooled by bringing the low temperature end of the helium refrigerator 23 into thermal contact with the storage chamber 42, where it is liquefied and the shroud 24a, 24b
Since the shroud is circulated, the temperature of the shroud can be maintained almost uniformly even if the shroud becomes large, and there is no need to be restricted by the position relative to the helium refrigerator 23. Of course, in this case, the nitrogen gas for shroud cooling is reliquefied in the helium refrigerator, so running costs do not increase.
本発明によれば、シユラウドの冷却をヘリウム
冷凍機で行うことができるので、ランニングコス
トを低減できる上に作業が簡単になり、かつ、ク
ライオポンプやシユラウドを冷却する複数台のヘ
リウム冷凍機を1台のヘリウム圧縮機に連結して
運転できるので、経済的になるという効果があ
る。
According to the present invention, since the shroud can be cooled by a helium refrigerator, running costs can be reduced and work is simplified, and multiple helium refrigerators for cooling the cryopump and shroud can be combined into one. Since it can be operated in conjunction with a single helium compressor, it has the effect of being economical.
第1図は従来の半導体薄膜生成装置の構成を示
す系統図、第2図は本発明の真空排気装置を有す
る半導体薄膜生成装置の系統図、第3図はクライ
オポンプの一般的な構造を示す断面図、第4図は
本発明の他の実施例による半導体薄膜生成装置の
系統図、第5図は本発明のさらに別の実施例によ
る半導体薄膜生成装置の系統図である。
1……試料交換室、2……真空バルブ、3……
高真空ポンプ、4……リークバルブ、5……ロー
タリーポンプ、6……試料準備・分析室、7……
薄膜成長室、8,9,10,11……ゲートバル
ブ、14……試料基板ホルダー、15……マニピ
ユレータ、16……素材供給源、21,22……
クライオポンプ、23……1段式ヘリウム冷凍
機、24a,24b……シユラウド、27……ヘ
リウム圧縮機、28,29……ヘリウム冷凍機。
Fig. 1 is a system diagram showing the configuration of a conventional semiconductor thin film production device, Fig. 2 is a system diagram of a semiconductor thin film production device having a vacuum evacuation device of the present invention, and Fig. 3 shows the general structure of a cryopump. 4 is a system diagram of a semiconductor thin film production apparatus according to another embodiment of the present invention, and FIG. 5 is a system diagram of a semiconductor thin film production apparatus according to still another embodiment of the present invention. 1...Sample exchange room, 2...Vacuum valve, 3...
High vacuum pump, 4...Leak valve, 5...Rotary pump, 6...Sample preparation/analysis room, 7...
Thin film growth chamber, 8, 9, 10, 11... gate valve, 14... sample substrate holder, 15... manipulator, 16... material supply source, 21, 22...
Cryopump, 23... Single-stage helium refrigerator, 24a, 24b... Shroud, 27... Helium compressor, 28, 29... Helium refrigerator.
Claims (1)
ら構成され、少くとも一方の真空槽には基板上に
半導体の薄膜を生成させるための素材供給源、試
料基板の保持移動を行うためのマニピユレータお
よび半導体材料の浮遊ガスを凝縮吸着させるため
のシユラウド等を備えた半導体薄膜生成装置にお
いて、少くとも一つの真空槽の排気用としてヘリ
ウム冷凍機付クライオポンプを設け、シユラウド
の冷却用としてヘリウム冷凍機を設け、上記クラ
イオポンプ用ヘリウム冷凍機とシユラウド冷却用
ヘリウム冷凍機を1台のヘリウム圧縮機に接続し
たことを特徴とする真空排気装置。 2 ヘリウム圧縮機とヘリウム冷凍機を結ぶ配管
にヘリウムガス流量調整手段を備えたことを特徴
とする特許請求の範囲第1項記載の真空排気装
置。 3 各ヘリウム冷凍機に往復周波数制御手段を備
えたことを特徴とする特許請求の範囲第1項記載
の真空排気装置。 4 シユラウドの一部に蒸発窒素ガス貯蔵室を設
け、該窒素ガス貯蔵室にヘリウム冷凍機の低温端
を熱的に接触させたことを特徴とする特許請求の
範囲第1項記載の真空排気装置。 5 クライオポンプに2段式ヘリウム冷凍機を備
え、一方、シユラウドに1段式ヘリウム冷凍機を
装着したことを特徴とする特許請求の範囲第1項
記載の真空排気装置。[Claims] 1. Consisting of a plurality of vacuum chambers and a gate valve connecting them, at least one of the vacuum chambers has a material supply source for producing a semiconductor thin film on a substrate, and a source for holding and moving a sample substrate. In a semiconductor thin film production apparatus that is equipped with a manipulator for performing the process and a shroud for condensing and adsorbing the floating gas of the semiconductor material, a cryopump with a helium refrigerator is provided for evacuating at least one vacuum chamber, and a cryopump with a helium refrigerator is provided for cooling the shroud. A vacuum evacuation device characterized in that a helium refrigerator is provided as a helium refrigerator, and the helium refrigerator for cryopump and the helium refrigerator for shroud cooling are connected to one helium compressor. 2. The vacuum evacuation device according to claim 1, characterized in that a pipe connecting the helium compressor and the helium refrigerator is provided with a helium gas flow rate adjusting means. 3. The vacuum evacuation device according to claim 1, wherein each helium refrigerator is provided with reciprocating frequency control means. 4. The vacuum evacuation device according to claim 1, characterized in that an evaporated nitrogen gas storage chamber is provided in a part of the shroud, and a low temperature end of a helium refrigerator is brought into thermal contact with the nitrogen gas storage chamber. . 5. The evacuation device according to claim 1, wherein the cryopump is equipped with a two-stage helium refrigerator, and the shroud is equipped with a single-stage helium refrigerator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8572083A JPS59211778A (en) | 1983-05-18 | 1983-05-18 | Vacuum exhaust equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8572083A JPS59211778A (en) | 1983-05-18 | 1983-05-18 | Vacuum exhaust equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59211778A JPS59211778A (en) | 1984-11-30 |
| JPS6310310B2 true JPS6310310B2 (en) | 1988-03-05 |
Family
ID=13866671
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8572083A Granted JPS59211778A (en) | 1983-05-18 | 1983-05-18 | Vacuum exhaust equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59211778A (en) |
-
1983
- 1983-05-18 JP JP8572083A patent/JPS59211778A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59211778A (en) | 1984-11-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4614093A (en) | Method of starting and/or regenerating a cryopump and a cryopump therefor | |
| JP4297975B2 (en) | Regeneration method by purging cryopump and reducing vacuum, cryopump and control device | |
| US5357760A (en) | Hybrid cryogenic vacuum pump apparatus and method of operation | |
| JPS60222572A (en) | Cryopump | |
| JPH0216377A (en) | Cryopump | |
| US6223540B1 (en) | Gas processing techniques | |
| JP3623659B2 (en) | Cryopump | |
| JPS6310310B2 (en) | ||
| JP2004071723A (en) | Vacuum processing device and its operation method | |
| JP2012530372A (en) | Apparatus for depositing a thin film of material on a substrate and method for regenerating such an apparatus | |
| JP3961050B2 (en) | Vacuum exhaust device | |
| JPH06346848A (en) | Regenerating cryopump method and evacuation system thereof | |
| JP4301532B2 (en) | Cryopump regeneration method | |
| JP2002070737A (en) | Regenerating method of cryopump | |
| JP3156409B2 (en) | Evacuation system | |
| JPS6328203Y2 (en) | ||
| JP3172767B2 (en) | Selective gas exhaust method | |
| JP2946733B2 (en) | Vacuum exhaust device | |
| JPH05195952A (en) | Cryopanel device | |
| Visser et al. | 1.18 A versatile cryopump for industrial vacuum systems | |
| JP2012509442A (en) | Process chamber with built-in exhaust system | |
| JPS6040497B2 (en) | Vacuum heat treatment furnace with highly clean atmosphere generation mechanism | |
| JPH01277687A (en) | Cryopump | |
| JP3130128B2 (en) | Vacuum pump with cryotrap | |
| JP2674591B2 (en) | Operating method of vacuum processing equipment |