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JPH0210864B2 - - Google Patents
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JPH0210864B2 - - Google Patents

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Publication number
JPH0210864B2
JPH0210864B2 JP20691386A JP20691386A JPH0210864B2 JP H0210864 B2 JPH0210864 B2 JP H0210864B2 JP 20691386 A JP20691386 A JP 20691386A JP 20691386 A JP20691386 A JP 20691386A JP H0210864 B2 JPH0210864 B2 JP H0210864B2
Authority
JP
Japan
Prior art keywords
substrate
susceptor
inert gas
heated
temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP20691386A
Other languages
Japanese (ja)
Other versions
JPS6365083A (en
Inventor
Takayuki Ooba
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fujitsu Ltd
Original Assignee
Fujitsu Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fujitsu Ltd filed Critical Fujitsu Ltd
Priority to JP20691386A priority Critical patent/JPS6365083A/en
Publication of JPS6365083A publication Critical patent/JPS6365083A/en
Publication of JPH0210864B2 publication Critical patent/JPH0210864B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 〔概要〕 気相成長装置内のヒータの熱を利用して不活性
ガスを加熱し、加熱された不活性ガスを基板の下
部から流し、基板の温度分布および装置内の圧力
変動による温度変化を小さく抑える。
[Detailed Description of the Invention] [Summary] The heat of the heater in the vapor phase growth apparatus is used to heat an inert gas, and the heated inert gas is flowed from the bottom of the substrate to change the temperature distribution of the substrate and the inside of the apparatus. Minimizes temperature changes due to pressure fluctuations.

〔産業上の利用分野〕[Industrial application field]

本発明は気相成長装置に関し、さらに詳しく言
えば、同装置における基板の加熱手段の改良に関
するものである。
TECHNICAL FIELD The present invention relates to a vapor phase growth apparatus, and more specifically, to an improvement in a means for heating a substrate in the same apparatus.

〔従来の技術〕 基板、例えばシリコンウエハ上にSiO2膜、シ
リコン窒化膜などの絶縁膜かW、Al、Ti、Mo等
の金属膜及びこれらのシリサイド膜を形成する場
合、化学気相成長(CVD)法で成膜することが
行われ、それには第5図に断面図で示される装置
が用いられる。同図において、11はチヤンバ、
12はアルミニウム(Al)またはステンレス
(SUS)製のサセプタ、13はウエハの如き基
板、14はガス供給部、15はヒータ、16は排
気管で、図示の装置は基板13をヒータ15から
の伝熱によつて加熱する抵抗加熱型である。ガス
供給部14は反応ガスを図に矢印で示す如くシヤ
ワー状に供給し、加熱された基板13上で化学的
な気相反応を発生して所定の膜が基板13上に成
長する。
[Prior Art] When forming an insulating film such as a SiO 2 film or a silicon nitride film, a metal film such as W, Al, Ti, Mo, or a silicide film of these films on a substrate such as a silicon wafer, chemical vapor deposition ( The film is formed by a CVD (CVD) method, and an apparatus shown in cross-section in FIG. 5 is used for this purpose. In the figure, 11 is a chamber;
12 is a susceptor made of aluminum (Al) or stainless steel (SUS), 13 is a substrate such as a wafer, 14 is a gas supply section, 15 is a heater, and 16 is an exhaust pipe. It is a resistance heating type that is heated by heat. The gas supply unit 14 supplies a reactive gas in a shower shape as shown by the arrow in the figure, and a chemical vapor phase reaction occurs on the heated substrate 13, so that a predetermined film grows on the substrate 13.

上記した抵抗加熱型の他には第6図に示される
IR加熱(ランプ加熱)型があり、この型の装置
ではサセプタ12aは石英で作られ、ランプ17
からの紫外線の輻射熱によつて基板13が加熱さ
れる構成となつている。
In addition to the resistance heating type mentioned above, there are other types shown in Figure 6.
There is an IR heating (lamp heating) type, and in this type of device the susceptor 12a is made of quartz and the lamp 17
The substrate 13 is heated by the radiant heat of ultraviolet rays from the substrate 13.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

従来の装置は基板との接触点における伝熱、輻
射熱などによる熱エネルギーの利用であつたた
め、接触面などの分布に依存した温度分布とな
り、気相成長の如く温度に敏感な反応では成長膜
の分布が一定にならない問題がある。すなわち、
熱エネルギーは、ヒータ15からサセプタ12
に、サセプタ12から基板13へと伝導するが、
この熱エネルギー伝導の均一性を得ることが難し
い。
Conventional equipment uses thermal energy through heat transfer or radiant heat at the point of contact with the substrate, so the temperature distribution depends on the distribution of the contact surface, etc., and in temperature-sensitive reactions such as vapor phase growth, the growth of the grown film There is a problem that the distribution is not constant. That is,
Thermal energy is transferred from the heater 15 to the susceptor 12
, conducts from the susceptor 12 to the substrate 13,
It is difficult to obtain uniformity in this thermal energy conduction.

また、基板は中心部分で最も温度が高く周縁に
向けて温度が下がり、周縁部分では中心部分より
も10℃も温度が低くなることがある。
Furthermore, the temperature of the substrate is highest at the center and decreases toward the periphery, where the temperature at the periphery can be as much as 10 degrees Celsius lower than at the center.

第6図に示したランプ加熱型においては、基板
13が置かれた部分以外の石英サセプタの表面に
膜が成長するだけでなく、基板とサセプタとの間
にもガスが侵入して膜が成長し、このような膜が
輻射熱の透過態様に影響して熱効率が悪くなる問
題がある。
In the lamp heating type shown in FIG. 6, a film not only grows on the surface of the quartz susceptor other than the part where the substrate 13 is placed, but also gas enters between the substrate and the susceptor and the film grows. However, there is a problem in that such a film affects the transmission mode of radiant heat, resulting in poor thermal efficiency.

また、成膜中にサセプタの基板が位置するとこ
ろ以外の第5図に符号18で示す周縁部にも膜が
成長し、その膜が剥がれて基板13上にゴミとし
て基板上に落ちて成長する膜の膜質を悪くする問
題もある。
Additionally, during film formation, a film grows on the peripheral area shown by reference numeral 18 in FIG. 5 other than where the susceptor substrate is located, and the film peels off and falls on the substrate 13 as dust and grows. There is also the problem of deteriorating the film quality of the film.

さらには、従来法ではチヤンバ内の伝熱媒体と
基板のサセプタとの接触面での加熱によつて基板
が加熱されるので、チヤンバ内の圧力が降下し伝
熱媒体が少なくなると基板温度が降下するという
圧力変動による基板温度の変化の問題もある。
Furthermore, in the conventional method, the substrate is heated by heating at the contact surface between the heat transfer medium in the chamber and the susceptor of the substrate, so when the pressure in the chamber decreases and the heat transfer medium decreases, the substrate temperature decreases. There is also the problem of changes in substrate temperature due to pressure fluctuations.

本発明はこのような点に鑑みて創作されたもの
で、温度分布を均一化し圧力の変化による温度変
化を抑えうる装置を提供することを目的とする。
The present invention was created in view of these points, and it is an object of the present invention to provide an apparatus that can uniformize temperature distribution and suppress temperature changes due to changes in pressure.

〔問題点を解決するための手段〕[Means for solving problems]

第1図は本発明実施例の断面図で、この実施例
は第5図の加熱手段が変更されたものであり、2
1はサセプタ、22は不活性ガス加熱管である。
FIG. 1 is a sectional view of an embodiment of the present invention, in which the heating means of FIG. 5 is modified, and 2
1 is a susceptor, and 22 is an inert gas heating tube.

本発明においては、ヒータ15を利用して不活
性ガス加熱管22を通る不活性ガス(He、Arな
ど)を加熱し、この加熱した不活性ガスを基板1
3の下部から流すもので、そのためには、サセプ
タ21の中央に連結する1または複数の細孔を作
り、この細孔から加熱した不活性ガスを噴出する
か、またはサセプタ21の表面に中央から外方に
放射状に延びる溝を形成し、この溝に沿つて加熱
不活性ガスが流れるようにする。
In the present invention, the heater 15 is used to heat the inert gas (He, Ar, etc.) passing through the inert gas heating tube 22, and the heated inert gas is transferred to the substrate 1.
For this purpose, one or more pores connected to the center of the susceptor 21 are made and heated inert gas is spouted from the pores, or heated inert gas is flowed from the center onto the surface of the susceptor 21. Grooves extending radially outward are formed along which the heated inert gas flows.

〔作用〕[Effect]

上記した装置においては、加熱された不活性ガ
スが基板13の下方から均一に流されるので、基
板は全体にわたつて均一に加熱されるものであ
る。
In the above-described apparatus, the heated inert gas is uniformly flowed from below the substrate 13, so that the entire substrate is uniformly heated.

〔実施例〕 以下、図面を参照して本発明の実施例を詳細に
説明する。
[Embodiments] Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

再び第1図を参照すると、ヒータ15は従来例
と同じものであるが、そのヒータ15のまわりに
He、Arなどの如き不活性ガスを通す不活性ガス
加熱管を配置し、図に矢印Iで示す如く不活性ガ
スを流す。不活性ガスはヒータ15によつて加熱
された不活性ガス加熱管22内を通る間に加熱さ
れる。
Referring to FIG. 1 again, the heater 15 is the same as the conventional example, but around the heater 15
An inert gas heating tube for passing an inert gas such as He, Ar, etc. is arranged, and the inert gas is caused to flow as shown by arrow I in the figure. The inert gas is heated while passing through the inert gas heating tube 22 heated by the heater 15 .

第1図を参照すると、本発明実施例において、
基板13の直径(図に見てD1で示す長さ)は
100mm、サセプタ21の直径(図に見てD2で示
す長さ)は120mm、基板13の外縁とサセプタ2
1の突出部の内縁との間の図にg1で示す距離は
5mm、サセプタ21の前記突出部の図にg2で示
す幅は5mm、不活性ガス加熱管22の図にnで示
す巻数n=10〜100、同加熱管の図にdで示す外
径は1/8インチ(約0.32cm)、また穴23の上方端
部と基板13の底面との間の図にhで示す距離は
5〜10mmにそれぞれ設定した。また、第2図aの
B−B線拡大断面図である第2図bに示されるよ
うに、溝24bの深さdと幅wはそれぞれ5mm
に、溝24aの溝24bに接する部分での溝24
aの幅〇は5mmに、またサセプタ21の外縁の突
出部の幅g2は前記したように5mmに設定した。
Referring to FIG. 1, in an embodiment of the present invention,
The diameter of the substrate 13 (the length indicated by D1 in the figure) is
100 mm, the diameter of the susceptor 21 (length indicated by D2 in the figure) is 120 mm, the outer edge of the substrate 13 and the susceptor 2
The distance between the inner edge of the protrusion of the susceptor 21 and the inner edge of the protrusion shown in the figure as g1 is 5 mm, the width of the protrusion of the susceptor 21 as g2 in the figure is 5 mm, and the number of turns of the inert gas heating tube 22 is n= 10 to 100, the outer diameter of the heating tube shown as d in the figure is 1/8 inch (approximately 0.32 cm), and the distance between the upper end of the hole 23 and the bottom surface of the substrate 13, shown as h in the figure, is 5 Each was set to ~10 mm. Further, as shown in FIG. 2b, which is an enlarged cross-sectional view taken along line B-B in FIG. 2a, the depth d and width w of the groove 24b are each 5 mm.
In addition, the groove 24 at the part of the groove 24a that contacts the groove 24b
The width 〇 of a was set to 5 mm, and the width g2 of the protrusion at the outer edge of the susceptor 21 was set to 5 mm as described above.

加熱された不活性ガスはサセプタの中央に設け
た穴23から図に矢印で示す如く四方に飛散し
て、基板13をその下側から均一に加熱する。穴
23は第1図に示す如く中央に1つ設けるか、ま
たはサセプタの中心以外の部分に平均的に複数個
配設してもよい。図示の実施例ではArまたはHe
ガスを10〜100c.c./minの流量で供給した。
The heated inert gas is scattered from a hole 23 provided in the center of the susceptor in all directions as shown by the arrows in the figure, uniformly heating the substrate 13 from below. One hole 23 may be provided in the center as shown in FIG. 1, or a plurality of holes 23 may be provided on average in a portion other than the center of the susceptor. In the illustrated embodiment Ar or He
Gas was supplied at a flow rate of 10-100 c.c./min.

本発明の他の実施例において、加熱された不活
性ガスは、第2図に部分的に示されるサセプタ2
1の表面に中心から放射状に形成された溝24a
に沿つて周縁溝24bに向けて流れ、その過程で
溝24aから上昇して基板13をその下側から均
一に加熱する。図示の例で溝24aは1mmのオー
ダーで1度から数度の間隔に切り、基板の周縁が
周縁溝24bのほぼ中央に位置するよう配置し
た。
In another embodiment of the invention, the heated inert gas is transferred to the susceptor 2 shown partially in FIG.
Grooves 24a formed radially from the center on the surface of 1
It flows along the groove 24b toward the peripheral groove 24b, and in the process rises from the groove 24a, uniformly heating the substrate 13 from below. In the illustrated example, the grooves 24a are cut at intervals of 1 to several degrees on the order of 1 mm, and are arranged so that the peripheral edge of the substrate is positioned approximately at the center of the peripheral groove 24b.

上記に説明した2つの実施例は、第6図に示し
たランプ加熱型のものにも適用可能であつて、そ
の場合の相違は、ヒータが抵抗加熱型かランプ加
熱型かの相違だけである。
The two embodiments described above can also be applied to the lamp heating type shown in FIG. 6, and the only difference in that case is whether the heater is a resistance heating type or a lamp heating type. .

第1図の装置と従来例の装置を用いて基板を加
熱した場合の基板温度を放射状型温度計で測定し
た結果は第3図の線図に示され、同図において横
軸に基板上の位置をとり、Cは基板中心部、Eは
基板の縁部を示すもので、また縦軸には温度を℃
でとつた。実線Aは本発明装置を用いた場合で、
基板温度は基板の中心部、縁部およびその他の部
分で平均して300℃であつた。点線Bは従来例の
場合を示し、中心部と縁部での温度差T1は約10
℃もあつた。
The results of measuring the substrate temperature with a radial thermometer when the substrate is heated using the device in FIG. 1 and the conventional device are shown in the diagram in FIG. C is the center of the board, E is the edge of the board, and the vertical axis shows the temperature in °C.
I got it. Solid line A is when the device of the present invention is used;
The substrate temperature averaged 300° C. at the center, edges and other parts of the substrate. Dotted line B shows the case of the conventional example, where the temperature difference T1 between the center and the edge is approximately 10
It was also warm.

第4図aはチヤンバ内の圧力変動と基板温度の
変動の関係を示す線図で、同図で横軸には時間を
とり、縦軸には温度を℃でとつた。横軸上の点X
はチヤンバ内の圧力が1Torrから0.1Torrに変つ
た点で、圧力が0.1Torrに下がつた理由はチヤン
バ内にHeガスが10c.c./minの流量で供給され始
めたからである。実線Yは本発明の場合で、圧力
の変動があつても基板温度は一定の温度300℃に
保たれたが、点線Zで示す従来例においては圧力
降下に伴つて基板温度が降下し、本発明の場合に
比べてT2=20℃の温度降下があつた。
FIG. 4a is a diagram showing the relationship between pressure fluctuations within the chamber and substrate temperature fluctuations, in which the horizontal axis represents time and the vertical axis represents temperature in °C. Point X on the horizontal axis
is the point where the pressure inside the chamber changed from 1 Torr to 0.1 Torr, and the reason why the pressure dropped to 0.1 Torr is because He gas started to be supplied into the chamber at a flow rate of 10 c.c./min. The solid line Y represents the case of the present invention, in which the substrate temperature was maintained at a constant temperature of 300°C even when the pressure fluctuated, whereas in the conventional example shown by the dotted line Z, the substrate temperature decreased as the pressure decreased, and the present invention There was a temperature drop of T2=20°C compared to the case of the invention.

本発明の一実施例で、第1図に示した装置を真
空チヤンバ内に配置し、WF6ガスを10sccm、
SiH4ガスを5sccm、H2ガスを200sccm、Heガス
を10sccmの流量で、それぞれマスフローコント
ローラを通して真空チヤンバ内に供給し、基板温
度400℃、真空チヤンバ内の圧力を0.1〜10Torr
の範囲内に設定してタングステンシリサイド膜を
成長した。そのときのプロセスは第4図bに示さ
れ、同図で横軸には時間tをとり、圧力、温度、
H2の供給のONとOFF、WF6とSiH4のONと
OFFの関係をそれぞれ線A,B,C,Dで現わ
す。この条件で成膜して膜圧分布は5%以下に抑
えることができたが、従来法では膜圧分布は10%
以下に抑えることができなかつたものである。上
記したプロセスで、Heは常時供給したために、
プロセスの初期の段階で圧力は0.1Torrになり、
このときHeの分圧は全圧と一致した。ソースガ
ス(WF6、SiH4)を線Dに示されるようにON、
OFFしたために圧力は線Aに示されるように変
化した。
In one embodiment of the present invention, the apparatus shown in FIG. 1 is placed in a vacuum chamber, and WF 6 gas is supplied at 10 sccm,
Supply SiH 4 gas at a flow rate of 5 sccm, H 2 gas at 200 sccm, and He gas at a flow rate of 10 sccm into the vacuum chamber through a mass flow controller, and adjust the substrate temperature to 400°C and the pressure in the vacuum chamber to 0.1 to 10 Torr.
The tungsten silicide film was grown by setting the temperature within the range of . The process at that time is shown in Figure 4b, in which time t is plotted on the horizontal axis, pressure, temperature,
H2 supply ON and OFF, WF 6 and SiH 4 ON and
The OFF relationships are represented by lines A, B, C, and D, respectively. By forming the film under these conditions, we were able to suppress the film pressure distribution to 5% or less, but with the conventional method, the film pressure distribution was 10%.
It was impossible to reduce the amount below. In the above process, since He was constantly supplied,
At the initial stage of the process the pressure is 0.1Torr,
At this time, the partial pressure of He matched the total pressure. Turn on the source gas (WF 6 , SiH 4 ) as shown by line D,
Since the switch was turned off, the pressure changed as shown by line A.

なお、第5図で示したサセプタの縁部分18に
おける膜の成長は認められず、従来問題となつた
ゴミ発生の問題が解決され、他方ランプ型の装置
において、石英のサセプタ上への膜の成長が発生
せず、伝熱効率が損なわれないことが確認され
た。
Incidentally, no film growth was observed on the edge portion 18 of the susceptor shown in FIG. 5, and the conventional problem of dust generation was solved. It was confirmed that no growth occurred and the heat transfer efficiency was not impaired.

〔発明の効果〕〔Effect of the invention〕

以上述べてきたように本発明によれば、He、
Arの如き不活性ガスが均一な熱源となるので基
板が一定の温度に保たれ、サセプタから不活性
ガスが流出するので、サセプタの表面には成膜す
ることがなく、ゴミの発生とか伝熱効率の低下が
防止され、チヤンバ内の圧力変動よる基板の温
度変化も防止され、半導体装置製造の歩留りと信
頼性向上に有効である。
As described above, according to the present invention, He,
Since the inert gas such as Ar serves as a uniform heat source, the substrate is kept at a constant temperature, and since the inert gas flows out from the susceptor, there is no film formation on the surface of the susceptor, which reduces dust generation and heat transfer efficiency. This prevents a decrease in the temperature of the substrate, and also prevents changes in the temperature of the substrate due to pressure fluctuations within the chamber, which is effective in improving the yield and reliability of semiconductor device manufacturing.

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

第1図は本発明実施例断面図、第2図は本願発
明によるサセプタ表面の部分的な図で、そのaは
平面図、そのbは同図aのB−B線拡大断面図、
第3図は本発明と従来例における基板温度を示す
線図、第4図aは本発明と従来例における装置の
圧力変動と基板温度の関係を示す線図、同図bは
本発明のプロセスにおける圧力、温度の変化、ガ
ス供給のONとOFFを示す線図、第5図は従来例
断面図、第6図は従来例の一部の断面図である。 第1図、第2図、第5図、第6図において、1
1はチヤンバ、12と12aはサセプタ、13は
基板、14は反応ガス供給部、15はヒータ、1
6は排気管、17はランプ、18はサセプタの縁
部分、21はサセプタ、22は不活性ガス加熱
管、23は穴、24aと24bは溝である。
FIG. 1 is a sectional view of an embodiment of the present invention, and FIG. 2 is a partial view of the surface of a susceptor according to the present invention, in which a is a plan view, b is an enlarged sectional view taken along the line B-B in the figure a, and FIG.
FIG. 3 is a diagram showing the substrate temperature in the present invention and the conventional example, FIG. 4 a is a diagram showing the relationship between the pressure fluctuation of the device and the substrate temperature in the present invention and the conventional example, and FIG. Fig. 5 is a sectional view of a conventional example, and Fig. 6 is a sectional view of a part of the conventional example. In Figures 1, 2, 5, and 6, 1
1 is a chamber, 12 and 12a are susceptors, 13 is a substrate, 14 is a reaction gas supply section, 15 is a heater, 1
6 is an exhaust pipe, 17 is a lamp, 18 is an edge portion of a susceptor, 21 is a susceptor, 22 is an inert gas heating tube, 23 is a hole, and 24a and 24b are grooves.

Claims (1)

【特許請求の範囲】 1 チヤンバ11内で加熱された基板13上に化
学気相成長法で成膜する装置において、 不活性ガス加熱管22をヒータ15のまわりに
配設し、 加熱された不活性ガスをサセプタ21に設けた
穴23を通しサセプタ上の基板13に吹き付けて
基板13を加熱する構成としたことを特徴とする
気相成長装置。 2 前記穴が複数個形成されてなる特許請求の範
囲第1項記載の装置。 3 前記ヒータがランプ17である特許請求の範
囲第1項記載の装置。 4 サセプタ21に溝24a,24bを設け、加
熱された不活性ガスがこれらの溝を通つて流れる
構成とした特許請求の範囲第1項記載の装置。
[Claims] 1. In an apparatus for forming a film by chemical vapor deposition on a substrate 13 heated within a chamber 11, an inert gas heating tube 22 is disposed around a heater 15, and a heated inert gas A vapor phase growth apparatus characterized in that the substrate 13 is heated by spraying active gas onto the substrate 13 on the susceptor through a hole 23 provided in the susceptor 21. 2. The device according to claim 1, wherein a plurality of the holes are formed. 3. The device according to claim 1, wherein the heater is a lamp 17. 4. The device according to claim 1, wherein grooves 24a and 24b are provided in the susceptor 21, and the heated inert gas flows through these grooves.
JP20691386A 1986-09-04 1986-09-04 Vapor growing apparatus Granted JPS6365083A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20691386A JPS6365083A (en) 1986-09-04 1986-09-04 Vapor growing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20691386A JPS6365083A (en) 1986-09-04 1986-09-04 Vapor growing apparatus

Publications (2)

Publication Number Publication Date
JPS6365083A JPS6365083A (en) 1988-03-23
JPH0210864B2 true JPH0210864B2 (en) 1990-03-09

Family

ID=16531153

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20691386A Granted JPS6365083A (en) 1986-09-04 1986-09-04 Vapor growing apparatus

Country Status (1)

Country Link
JP (1) JPS6365083A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2522402B2 (en) * 1989-08-24 1996-08-07 日本電気株式会社 Wafer heating device

Also Published As

Publication number Publication date
JPS6365083A (en) 1988-03-23

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