JPH0463153B2 - - Google Patents
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- JPH0463153B2 JPH0463153B2 JP9572187A JP9572187A JPH0463153B2 JP H0463153 B2 JPH0463153 B2 JP H0463153B2 JP 9572187 A JP9572187 A JP 9572187A JP 9572187 A JP9572187 A JP 9572187A JP H0463153 B2 JPH0463153 B2 JP H0463153B2
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- gas
- cylindrical body
- supply device
- plate
- gas supply
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Description
【発明の詳細な説明】
〔概要〕
シヤワー状にガスを流出する機能を有するガス
供給装置の内部にガス案内板を用いて層流形成手
段を設けて、導入ガスを中心部から周辺部に向か
う層流に形成して該装置内を誘導しガス流出面に
配設されたガス拡散板上に周辺部から供給するよ
うにして装置内を通過するガスの流れを低温部か
ら高温部に向かう一方向の流れに統一し、これに
よつて気相成長の際ガス供給装置内に生成堆積す
る粉末状反応生成物の量を減少せしめて、該粉末
状反応生成物の落下による被成長基板面の汚染を
防止する。[Detailed Description of the Invention] [Summary] A laminar flow forming means is provided using a gas guide plate inside a gas supply device that has a function of discharging gas in a shower shape, and the introduced gas is directed from the center to the periphery. The flow of gas passing through the device is directed from a low-temperature part to a high-temperature part by forming a laminar flow inside the device and supplying it from the periphery onto a gas diffusion plate disposed on the gas outflow surface. This reduces the amount of powdery reaction products generated and deposited in the gas supply device during vapor phase growth, and prevents the surface of the substrate to be grown due to falling of the powdery reaction products. Prevent contamination.
本発明は気相反応において被処理基板上に反応
ガスを注下するのに用いられるガス供給装置に係
り、特に化学気相成長に際して成長膜質の向上に
寄与するガス供給装置に関する。
The present invention relates to a gas supply device used to inject a reactive gas onto a substrate to be processed in a vapor phase reaction, and particularly to a gas supply device that contributes to improving the quality of a grown film during chemical vapor deposition.
半導体IC等に用いられるに二酸化シリコン
(SiO2)、燐珪酸ガラス(PSG)等の層間絶縁膜
は、主として化学気相成長(CVD)法によつて
形成されるが、近時該半導体ICの高集積化に伴
つて該層間絶縁膜が薄く形成され、且つ該層間絶
縁膜上に形成される配線層の膜厚も薄く形成され
るようになつて来て、膜質の低下による該層間絶
縁膜の絶縁性の劣化や、該層間絶縁膜の突起状欠
陥に起因する配線層の断線等が問題になつてい
る。 Interlayer insulating films such as silicon dioxide (SiO 2 ) and phosphosilicate glass (PSG) used in semiconductor ICs are mainly formed by chemical vapor deposition (CVD). With higher integration, the interlayer insulating film is becoming thinner, and the wiring layer formed on the interlayer insulating film is also becoming thinner, resulting in a decrease in the quality of the interlayer insulating film. Problems include deterioration of the insulation properties of the interlayer insulating film and disconnection of the wiring layer due to protruding defects in the interlayer insulating film.
この層間絶縁膜の膜質劣化や突起状欠陥は、多
くは該層間絶縁膜を形成するCVD装置に起因す
るもので、高集積度ICの信頼性向上の面から、
その改善が要望されている。 This deterioration in film quality and protruding defects in the interlayer insulating film are mostly caused by the CVD equipment that forms the interlayer insulating film, and from the perspective of improving the reliability of highly integrated ICs,
Improvements are requested.
第2図は上記層間絶縁膜の形成に多く用いられ
る従来の減圧CVD装置の模式側断面図で、図中、
51は成長室、52はガス供給管、53はガス供
給装置、54は真空排気口、55はヒータを内蔵
した基板支持台、56は被成長基板を示す。
FIG. 2 is a schematic side sectional view of a conventional low pressure CVD apparatus often used for forming the above-mentioned interlayer insulating film.
51 is a growth chamber, 52 is a gas supply pipe, 53 is a gas supply device, 54 is a vacuum exhaust port, 55 is a substrate support with a built-in heater, and 56 is a substrate to be grown.
上記従来のCVD装置に配設されたシヤワー状
にガスを流出するガス供給装置即ちシヤワー状ガ
ス供給装置53は、第3図に示す模式側断面図の
ように、軸に対して直角な上下端面を有する高さ
の低い円筒体57と、その上端面に固着された中
心部にガス供給管52が開口固定された天板58
と、円筒体57の下端面の近傍に該端面と平行に
固着された第1のガス流通孔59を低配設密度で
有する第1のガス拡散板60と、該円筒体57の
下端面に固着された第2のガス流通孔61を高配
設密度で有する第2のガス拡散板62とによつて
構成されていた。 As shown in the schematic side sectional view shown in FIG. A top plate 58 having a gas supply pipe 52 opened and fixed in the center fixed to the upper end surface of the cylinder body 57
and a first gas diffusion plate 60 having first gas flow holes 59 fixed near the lower end surface of the cylindrical body 57 in parallel with the end surface at a low density; A second gas diffusion plate 62 has fixed second gas flow holes 61 arranged at a high density.
しかし該従来構造のシヤワー状ガス供給装置に
おいては、ガス供給管52から例えばモノシラン
(SiH4)と酸素(O2)との混合ガスよりなる成長
ガスを導入して、例えば400℃程度に加熱された
被成長基板56上にSiO2膜を成長しようとする
際、基板支持台55及び被成長基板56からの輻
射熱によつて高温に加熱されている第1のガス拡
散板60の中央部に常温の成長ガス63が高速で
衝突して該ガス拡散板60が局部的に冷却され、
その近傍に低温領域64が形成される。 However, in the shower-like gas supply device of the conventional structure, a growth gas made of a mixed gas of, for example, monosilane (SiH 4 ) and oxygen (O 2 ) is introduced from the gas supply pipe 52 and heated to, for example, about 400°C. When attempting to grow a SiO 2 film on the growth substrate 56, the central part of the first gas diffusion plate 60, which is heated to a high temperature by radiant heat from the substrate support 55 and the growth substrate 56, is heated to room temperature. The growth gas 63 collides at high speed to locally cool the gas diffusion plate 60,
A low temperature region 64 is formed in the vicinity thereof.
そしてガス拡散板60の周辺部に接する高温領
域65から、該高温において飽和状態に反応種が
形成された高温の成長ガスの一部が鎖線で示す矢
印66のように低温領域64へ逆流し、冷却され
て反応種が急激に過飽和状態になり、粉末状の
SiO2を生成して、該SiO2粉67を拡散板60,
62上等に堆積させる。 Then, from the high temperature region 65 in contact with the peripheral portion of the gas diffusion plate 60, a part of the high temperature growth gas in which reactive species are formed in a saturated state at the high temperature flows back to the low temperature region 64 as indicated by an arrow 66 indicated by a chain line. Upon cooling, the reactive species rapidly become supersaturated, forming a powdery state.
Generate SiO 2 and transfer the SiO 2 powder 67 to the diffusion plate 60,
62, etc.
また特に成長ガスの導入を停止した際には円筒
体57と第1のガス拡散板60とによつて画定さ
れる一空間内に停滞している成長ガスが該空間内
を自由に移動し、高温の成長ガスが低温領域に浸
入し冷却されるので、上記SiO2粉67の堆積は
より顕著となる。 In addition, especially when the introduction of the growth gas is stopped, the growth gas stagnant in a space defined by the cylindrical body 57 and the first gas diffusion plate 60 moves freely within the space, Since the high-temperature growth gas enters the low-temperature region and is cooled, the deposition of the SiO 2 powder 67 becomes more significant.
そしてこれらSiO2粉67は、成長ガスを流通
せしめた際に成長ガス62に載つて被成長基板5
6上に運ばれ該基板上に付着するので、該基板5
6上に成長するSiO2膜68に亀裂状の欠陥69
や、突起状の欠陥70を発生させ、これによつて
該SiO2膜68による層間絶縁膜の絶縁性の劣化
や、該SiO2層間絶縁膜上に形成される金属配線
層の断線等が生ずる。 These SiO 2 powders 67 are placed on the growth gas 62 when the growth gas is passed through the growth substrate 5.
6 and adheres to the substrate, so that the substrate 5
Crack-like defects 69 in the SiO 2 film 68 grown on 6
and protruding defects 70 are generated, which causes deterioration of the insulation properties of the interlayer insulating film by the SiO 2 film 68 and disconnection of the metal wiring layer formed on the SiO 2 interlayer insulating film. .
そこで従来は、上記欠陥を防止して半導体IC
等の製造デバイスの信頼性を向上させるために、
該ガス供給装置の洗浄が頻繁に行われたので、
CVD装置の保守工数の増大、スループツトの大
幅な減少等が問題となつていた。 Therefore, in the past, the above defects were prevented and semiconductor IC
In order to improve the reliability of manufactured devices such as
Because the gas supply equipment was cleaned frequently,
Problems include an increase in maintenance man-hours for CVD equipment and a significant decrease in throughput.
本発明が解決しようとする問題点は、上記のよ
うに従来のガス供給装置を具備したCVD装置に
おいては、気相成長絶縁膜の亀裂状或いは突起状
の欠陥による絶縁性の劣化や、配線層の断線等に
よる製造デバイスの信頼性の低下を防止するため
に、ガス供給装置の頻繁な洗浄が必要なために
CVD装置の保守工数が増大し、且つスループツ
トが大幅に減少していたことである。
The problems to be solved by the present invention are that, as mentioned above, in CVD equipment equipped with a conventional gas supply device, insulation deteriorates due to crack-like or protruding defects in the vapor-grown insulating film, and wiring layer Gas supply equipment requires frequent cleaning to prevent reliability degradation of manufacturing devices due to wire breakage, etc.
The maintenance man-hours for CVD equipment increased and the throughput decreased significantly.
上記問題点は、軸に対して直角な上下端面を有
する円筒体と、該円筒体の上端面に固着された中
心部にガス導入口を有する天板と、該円筒体の下
端面に固着されたガス拡散板と、該円筒体の内部
に、該円筒体の側壁との間に間隙部を有するガス
案内板を用いて構成されガス導入口から導入され
るガスを該円筒体の中心部から周辺部に向かう層
流に形成する層流形成手段とを有し、ガス導入口
から導入されたガスが該層流形成手段を経て該ガ
ス案内板と円筒体側壁との間隙部から該拡散板上
に供給され、該ガス拡散板を介して外部に流出せ
しめられることを特徴とする本発明によるガス供
給装置によつて解決される。
The above problem consists of a cylindrical body having upper and lower end faces perpendicular to the axis, a top plate having a gas inlet in the center fixed to the upper end face of the cylinder, and a top plate fixed to the lower end face of the cylinder. The gas guide plate is configured by using a gas diffusion plate having a gap between the inside of the cylindrical body and a side wall of the cylindrical body, and directs the gas introduced from the gas inlet from the center of the cylindrical body. a laminar flow forming means for forming a laminar flow toward the peripheral portion, and the gas introduced from the gas inlet passes through the laminar flow forming means and passes through the gap between the gas guide plate and the side wall of the cylinder to the diffusion plate. This problem is solved by the gas supply device according to the present invention, which is characterized in that the gas is supplied to the top and is caused to flow out to the outside via the gas diffusion plate.
即ち本発明に係るシヤワー状のガス供給装置に
おいては、天板の中心部に開口する単数若しくは
同心円状の複数のガス導入口から導入される各々
のガスを個々に、天板及び装置内部に配設したガ
ス案内板によつて薄い層流にして装置の中心部か
ら周辺部に誘導し、装置の内壁面と案内板の周縁
部との間に形成される空隙部を介して周辺部から
ガス拡散板上に供給し、ガス拡散板を介してシヤ
ワー状に流出させる。
That is, in the shower-like gas supply device according to the present invention, each gas introduced from a single gas inlet or a plurality of concentric gas inlet openings in the center of the top plate is individually arranged inside the top plate and the device. The installed gas guide plate guides the gas from the center of the device to the periphery in a thin laminar flow, and the gas flows from the periphery through the gap formed between the inner wall of the device and the periphery of the guide plate. The gas is supplied onto the diffusion plate and flows out through the gas diffusion plate in the form of a shower.
このようにすることにより、ガス供給装置内を
流れるガスの流れが常温の導入ガスの衝突によつ
て冷却される最低温領域から該冷却を直接受けな
い装置の内壁近傍の中温領域を経て輻射により最
も高温に加熱されているガス拡散板に達する低温
部から高温部に向かう一方向の流れに統一される
ので、ガス中に含まれる反応種が過飽和になるこ
とがない。 By doing so, the gas flow inside the gas supply device is caused by radiation from the lowest temperature region where it is cooled by the collision of the introduced gas at room temperature, through the medium temperature region near the inner wall of the device that does not receive the cooling directly. Since the flow is unified in one direction from the low temperature part to the high temperature part reaching the gas diffusion plate heated to the highest temperature, the reactive species contained in the gas will not become supersaturated.
従つて気相成長に際して、過飽和反応種によつ
てガス供給装置内に生成堆積される粉末状の気相
成長物質は大幅に減少し、ガス供給装置から被成
長基板面に落下する粉末状の気相成長物質が減少
するので、気相成長膜の亀裂状欠陥及び突起状欠
陥が大幅に減少する。 Therefore, during vapor phase growth, the amount of powdery vapor grown material generated and deposited in the gas supply device by supersaturated reactive species is greatly reduced, and the amount of powdered vapor that falls from the gas supply device onto the surface of the substrate to be grown is reduced. Since the amount of phase grown material is reduced, crack-like defects and protrusion-like defects in the vapor grown film are significantly reduced.
以下本発明を、2個のガス導入口を有する一実
施例について、第1図に示す模式側断面図a及び
模式平面図bを用いて具体的に説明する。
The present invention will be specifically described below with reference to a schematic side sectional view a and a schematic plan view b shown in FIG. 1 for an embodiment having two gas inlets.
第1図において、
1は軸に対して直角な上下端面を有し石英等よ
りなる高さ例えば5〜10mm程度の円筒体、
2は円筒体1の上端面に固着された石英等より
なる天板、
3は天板2の中心部に開口して固定された石英
等よりなる第1のガス導入管、
4は石英等よりなり第1のガス導入管のほぼ中
心を貫通する第2のガス導入管、
5は第2のガス導入管4の先端部が中央部に開
口して固定され該第2のガス導入管4によつて円
筒体内1のほぼ中心位置に該円筒体2の上端面か
ら例えば1mm程度の距離d1を隔てて平行に支持さ
れた石英等よりなる第1のガス案内板、
6は図示されない支持手段により第1のガス案
内板5の下部に例えば1mm程度の距離d2を隔てて
平行に支持された石英等よりなる第2のガス案内
板、
7は第2のガス案内板6の下部に例えば1mm程
度の距離d3を隔てて平行に、該円筒体2の開口部
を覆つて固着された石英板等よりなり、例えば
0.3mmφのガス流出孔8が3mm程度のピツチでマ
トリクス上に配設されたガス拡散板、
9はガス流を示す矢印、
10はガス流出面
を示す。 In Fig. 1, 1 is a cylindrical body made of quartz or the like and having a height of about 5 to 10 mm, with upper and lower end surfaces perpendicular to the axis, and 2 is a ceiling made of quartz or the like fixed to the upper end surface of the cylindrical body 1. plate; 3 is a first gas introduction tube made of quartz or the like that opens and is fixed in the center of the top plate 2; 4 is a second gas introduction tube made of quartz or the like that passes through approximately the center of the first gas introduction tube; An introduction pipe 5 is a second gas introduction pipe 4 which is fixed with its distal end opening in the center, and the second gas introduction pipe 4 extends from the upper end surface of the cylindrical body 2 to approximately the center position of the cylindrical body 1. A first gas guide plate 6 made of quartz or the like is supported in parallel at a distance d1 of about 1 mm from the bottom of the first gas guide plate 5 by a support means (not shown). A second gas guide plate 7 made of quartz or the like is supported parallel to the cylindrical body 2 with a distance d3 of, for example, about 1 mm apart from the lower part of the second gas guide plate 6. It is made of a quartz plate etc. that is fixed to cover the opening, e.g.
A gas diffusion plate in which gas outlet holes 8 of 0.3 mmφ are arranged on a matrix at a pitch of about 3 mm, 9 indicates an arrow indicating a gas flow, and 10 indicates a gas outlet surface.
なお第1、第2のガス案内板5,6と円筒体1
の内側面との距離d4は、例えば2mm程度に形成さ
れる。 Note that the first and second gas guide plates 5 and 6 and the cylindrical body 1
The distance d 4 from the inner surface of the groove is, for example, about 2 mm.
上記本発明に係るガス供給装置を前述のような
反応容器内に、ガス拡散板7を有するガス流出面
10を例えば420℃程度に加熱された被成長基板
(図示せず)に対向させて配置し、第2のガス導
入管4から例えば500c.c./minの流量でO2ガスを
流入し、第1のガス導入管3からSiH4ガス50
c.c./minとキヤリアガスである窒素(N2)ガス
3l/minとの混合ガスを流入し、反応容器内を
10Torr程度に減圧して図示しない被成長基板上
に1μm程度の厚さのSiO2膜の成長を行つた。 The gas supply device according to the present invention is placed in the reaction vessel as described above, with the gas outflow surface 10 having the gas diffusion plate 7 facing a growth substrate (not shown) heated to, for example, about 420°C. Then, O 2 gas is introduced from the second gas introduction pipe 4 at a flow rate of, for example, 500 c.c./min, and SiH 4 gas is introduced from the first gas introduction pipe 3 at a flow rate of 500 c.c./min.
cc/min and carrier gas nitrogen (N 2 ) gas
A mixed gas of 3l/min flows into the reaction vessel.
A SiO 2 film with a thickness of about 1 μm was grown on a growth substrate (not shown) under reduced pressure to about 10 Torr.
この成長工程において、上記ガス供給装置の被
処理基板側からの輻射及び伝導熱によつて加熱さ
れてガス拡散板7と第2のガス案内板6との間の
第3の空間部が最も高い300℃程度の温度T3に加
熱され、該2のガス案内板6と第1のガス案内板
5との間の第2の空間部が250℃程度の温度T2に
加熱され、第1のガス案内板5と上端面との間の
第1の空間部が200℃程度の温度T1に加熱され
る。そして更に各空間部には、該空間に形成され
るガスの層流の向きと反対の向きの温度勾配が形
成される。また上記ガスの流入量に対して距離
d1,d2,d3で示される各空間部の高さが1mm程度
に十分低く形成されているので各空間部に形成さ
れる層流内に高温部から低温部に逆流する乱流を
しようずることがない。従つて該ガス供給装置内
の上記成長ガスの流れは低温から高温に向かう温
度勾配に沿つた流れのみとなるので、該装置の内
部に過飽和反応種に起因する粉末状SiO2の堆積
は殆ど生じなくなる。 In this growth process, the third space between the gas diffusion plate 7 and the second gas guide plate 6 is heated by the radiation and conduction heat from the substrate side of the gas supply device to be the highest. The second space between the second gas guide plate 6 and the first gas guide plate 5 is heated to a temperature T2 of about 250℃, and the first gas guide plate 6 is heated to a temperature T3 of about 300℃. The first space between the gas guide plate 5 and the upper end surface is heated to a temperature T1 of about 200°C. Furthermore, a temperature gradient is formed in each space in a direction opposite to the direction of the laminar flow of gas formed in the space. Also, the distance for the above gas inflow amount is
Since the height of each space indicated by d 1 , d 2 , and d 3 is formed sufficiently low to about 1 mm, turbulent flow flowing back from the high temperature part to the low temperature part is prevented from occurring in the laminar flow formed in each space. There's nothing I can do about it. Therefore, the flow of the growth gas in the gas supply device is only along the temperature gradient from low temperature to high temperature, so that almost no deposition of powdered SiO 2 due to supersaturated reactive species occurs inside the device. It disappears.
そのためこのガス供給装置において、洗浄を行
わずに厚さ1μmの上記SiO2膜の気相成長を30回
以上行つても成長膜にデバイスの信頼性を低下せ
しめる大きさ及び量の突起欠陥及び亀裂欠陥を生
ずることがなかつた。この値は従来装置において
10回毎に洗浄していたのに比べて大幅に改善され
た値であり、これによつてCVD装置のスループ
ツトは大幅に向上する。 Therefore, in this gas supply device, even if the vapor phase growth of the SiO 2 film with a thickness of 1 μm is performed 30 times or more without cleaning, protrusion defects and cracks of a size and amount that reduce the reliability of the device will occur in the grown film. No defects occurred. This value is
This is a significant improvement compared to cleaning every 10 times, and this greatly improves the throughput of the CVD equipment.
以上説明のように本発明によればガス供給装置
内に反応種を過飽和に含んだ反応ガスが形成され
ることがなくなるので、該ガス供給装置をCVD
装置に用いた際に該ガス供給装置内に粉末状の反
応生成物が生成堆積されることが極めて少なくな
るので、CVD膜の品質を確保するために行うガ
ス供給装置の洗浄頻度を大幅に減少することが出
来、CVD装置の保守工数の削減及びスループツ
トの向上が図れる。
As explained above, according to the present invention, a reactive gas supersaturated with reactive species is not formed in the gas supply device, so that the gas supply device can be used for CVD.
When used in the equipment, the generation and accumulation of powdered reaction products in the gas supply device is extremely reduced, so the frequency of cleaning the gas supply device to ensure the quality of CVD films is significantly reduced. It is possible to reduce maintenance man-hours and improve throughput for CVD equipment.
第1図は本発明の一実施例を模式的に示す側断
面図a及び平面図b、第2図は従来の減圧CVD
装置を示す模式側断面図、第3図は従来のガス供
給装置の模式側断面図である。
図において、1は円筒体、2は天板、3は第1
のガス導入管、4は第2のガス導入管、5は第1
のガス案内板、6は第2のガス案内板、7はガス
拡散板、8はガス流出孔、9はガス流を示す矢
印、10はガス流出面、を示す。
Fig. 1 is a side sectional view a and a plan view b schematically showing an embodiment of the present invention, and Fig. 2 is a conventional reduced pressure CVD.
A schematic side sectional view showing the device; FIG. 3 is a schematic side sectional view of a conventional gas supply device. In the figure, 1 is a cylindrical body, 2 is a top plate, and 3 is a first
, 4 is the second gas introduction pipe, and 5 is the first gas introduction pipe.
, 6 is a second gas guide plate, 7 is a gas diffusion plate, 8 is a gas outlet hole, 9 is an arrow indicating a gas flow, and 10 is a gas outlet surface.
Claims (1)
と、 該円筒体の上端面に固着された中心部にガス導
入口を有する天板と、 該円筒体の下端面に固着されたガス拡散板と、 該円筒体の内部に、該円筒体の側壁との間に間
隙を有するガス案内板を用いて構成されガス導入
口から導入されるガスを該円筒体の中心部から周
辺部に向かう層流に形成する層流形成手段とを有
し、 ガス導入口から導入されたガスが該層流形成手
段を経て該ガス案内板と円筒体側壁との間隙部か
ら該拡散板上に供給され、該ガス拡散板を介して
外部に流出せしめられることを特徴とするガス供
給装置。 2 上記ガス導入口が同心円状に形成された複数
のガス導入口よりなり、且つ上記層流形成手段が
各々のガス導入口から導入されるガスについて
個々に設けられてなることを特徴とする特許請求
の範囲第1項記載のガス供給装置。 3 上記ガス拡散板が、複数個のガス流出孔を有
する単数若しくは複数枚の平板よりなることを特
徴とする特許請求の範囲第1項記載のガス供給装
置。[Scope of Claims] 1. A cylindrical body having upper and lower end faces perpendicular to an axis, a top plate having a gas inlet in the center fixed to the upper end face of the cylindrical body, and a top plate having a gas inlet port at the center thereof, and a lower end face of the cylindrical body. A fixed gas diffusion plate and a gas guide plate having a gap inside the cylindrical body and a side wall of the cylindrical body are used to direct the gas introduced from the gas inlet into the center of the cylindrical body. and a laminar flow forming means for forming a laminar flow toward the peripheral area, and the gas introduced from the gas inlet passes through the laminar flow forming means and diffuses from the gap between the gas guide plate and the side wall of the cylindrical body. A gas supply device characterized in that the gas is supplied onto a plate and is caused to flow out through the gas diffusion plate. 2. A patent characterized in that the gas inlet is composed of a plurality of concentrically formed gas inlets, and the laminar flow forming means is provided individually for the gas introduced from each gas inlet. A gas supply device according to claim 1. 3. The gas supply device according to claim 1, wherein the gas diffusion plate is composed of one or more flat plates having a plurality of gas outflow holes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9572187A JPS63262469A (en) | 1987-04-17 | 1987-04-17 | Gas supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9572187A JPS63262469A (en) | 1987-04-17 | 1987-04-17 | Gas supply device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63262469A JPS63262469A (en) | 1988-10-28 |
| JPH0463153B2 true JPH0463153B2 (en) | 1992-10-08 |
Family
ID=14145339
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9572187A Granted JPS63262469A (en) | 1987-04-17 | 1987-04-17 | Gas supply device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63262469A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6245192B1 (en) | 1999-06-30 | 2001-06-12 | Lam Research Corporation | Gas distribution apparatus for semiconductor processing |
-
1987
- 1987-04-17 JP JP9572187A patent/JPS63262469A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63262469A (en) | 1988-10-28 |
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| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |