JPH09148259A - Lateral reactor - Google Patents

Lateral reactor

Info

Publication number
JPH09148259A
JPH09148259A JP30533695A JP30533695A JPH09148259A JP H09148259 A JPH09148259 A JP H09148259A JP 30533695 A JP30533695 A JP 30533695A JP 30533695 A JP30533695 A JP 30533695A JP H09148259 A JPH09148259 A JP H09148259A
Authority
JP
Japan
Prior art keywords
gas
furnace core
core tube
reaction
reaction gas
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.)
Pending
Application number
JP30533695A
Other languages
Japanese (ja)
Inventor
Shigeaki Ide
繁章 井手
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.)
NEC Kyushu Ltd
Original Assignee
NEC Kyushu 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 NEC Kyushu Ltd filed Critical NEC Kyushu Ltd
Priority to JP30533695A priority Critical patent/JPH09148259A/en
Publication of JPH09148259A publication Critical patent/JPH09148259A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To make uniform surface process of a wafer without requiring a movable mechanism being a dust source by a method wherein a plurality of exhaust ports are provided in a lower part of a furnace core tube opposite a plurality of gas blow-out ports which are arranged in an upper part of the furnace core tube, and which blow out reaction gas in a wafer column. SOLUTION: This lateral reactor is provided with a gas supply mechanism 1 arranged laterally with a plurality of gas blow-out ports 3a, 3b, 3c which are arranged in an upper part in a furnace core tube 6, and which introduce reaction gas; and a gas exhaust tube 2 provided with a gas exhaust port 4 which is arranged opposite gas blow-out ports 3a, 3b, 3c in a lower part in the furnace core tube, and which discharges reaction gas. The gas supply mechanism 1 comprises a plurality of gas introduction tubes 1a, 1b, 1c, and a flow volume valve is independently provided in each of the gas introduction tubes 1a, 1b, 1c so that a flow volume of reaction gas in the gas blow-out ports 3a, 3b, 3c is made constant.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、横方向に載置され
る長尺な炉芯管に挿入され高温加熱されるとともに反応
ガスの雰囲気のもとで半導体基板を酸化・拡散処理また
は多結晶シリコン膜,窒化膜等を成膜する横型反応装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a semiconductor substrate which is inserted in a long furnace core tube placed in a lateral direction and heated at a high temperature, and which is subjected to an oxidation / diffusion treatment or a polycrystalline process on a semiconductor substrate under an atmosphere of a reaction gas. The present invention relates to a horizontal reactor for forming a silicon film, a nitride film, etc.

【0002】[0002]

【従来の技術】従来、この種の横型反応装置は、半導体
基板(以下単にウェハと記す)の表面に酸化膜の形成や
不純物の拡散あるいは窒化膜や多結晶シリコンの形成な
どに用いられていた。しかしながら、このような表面処
理は時間がかかるため、より能率を良くするために複数
枚のウェハを同時に処理していた。
2. Description of the Related Art Conventionally, this type of horizontal reactor has been used for forming an oxide film, diffusing impurities, forming a nitride film or polycrystalline silicon on the surface of a semiconductor substrate (hereinafter simply referred to as a wafer). . However, since such a surface treatment takes time, a plurality of wafers are simultaneously treated in order to improve efficiency.

【0003】図2は従来の横型反応装置の一例を示す模
式断面図である。多数枚のウェハを処理する横型反応装
置は、図3に示すように、多数のウェハ14を一方向に
並べ載置するボート13を収納する炉芯管11と、この
炉芯管11の内部を高温加熱するヒータ12とを備えて
いる。そして、炉芯管11の一方より反応ガスを導入し
炉芯管11内を一定の圧力にしてから、酸化・拡散処理
または多結晶シリコン膜,窒化膜等の成長を行ってい
た。
FIG. 2 is a schematic sectional view showing an example of a conventional horizontal reactor. As shown in FIG. 3, a horizontal reactor for processing a large number of wafers includes a furnace core tube 11 for accommodating a boat 13 in which a large number of wafers 14 are placed side by side in one direction, and an inside of the furnace core tube 11. And a heater 12 for heating at a high temperature. Then, a reaction gas is introduced from one side of the furnace core tube 11 to make the inside of the furnace core tube 11 at a constant pressure, and then an oxidation / diffusion process or a growth of a polycrystalline silicon film, a nitride film or the like is performed.

【0004】しかしながら、この種の横型反応装置で
は、0.5Torr程度の圧力で粘性流の領域にかかわ
らずガス供給口に近い方が反応ガスの濃度が高く炉口側
では低くなる。その結果、ウェハ14と接触する反応ガ
スの活性分子にむらが生じ、ボート13に載置されたウ
ェハ14の間に表面処理のばらつきが生ずる恐れがあっ
た。
However, in this type of horizontal reactor, the concentration of the reaction gas is higher near the gas supply port and lower at the furnace port side regardless of the viscous flow region at a pressure of about 0.5 Torr. As a result, the active molecules of the reaction gas that come into contact with the wafer 14 become uneven, and there is a risk that variations in the surface treatment will occur among the wafers 14 mounted on the boat 13.

【0005】図3(a)および(b)は従来の横型反応
装置の他の例を示す縦断面図および横断面図である。膜
厚を均一に成長させるためにガス供給機構を改良した横
型反応装置の一種である気相成長装置として、特開昭5
8−25224号公報に開示されている。この横型反応
装置である気相成長装置は、図3に示すように、複数の
噴射口を有し反応管11aの内壁に沿って管内を移動し
ながら反応ガスを供給するガス供給管10を反応管内に
備えている。
3 (a) and 3 (b) are a longitudinal sectional view and a lateral sectional view showing another example of a conventional horizontal reactor. As a vapor phase growth apparatus which is a kind of a horizontal reactor in which a gas supply mechanism is improved in order to uniformly grow a film thickness, Japanese Patent Application Laid-Open No. Sho 5 (1999)
It is disclosed in Japanese Unexamined Patent Publication No. 8-25224. As shown in FIG. 3, the vapor phase growth apparatus, which is a horizontal reactor, reacts a gas supply pipe 10 which has a plurality of injection ports and which supplies a reaction gas while moving along the inner wall of the reaction pipe 11a. Prepared in the pipe.

【0006】そして、この気相成長装置では、ガス供給
管10からのガスの噴射方向を反応管の軸中心から10
°ないし30°外れた方向の角度をもって管内を移動し
ながらガスを噴射することにより、サセプタ9に載置さ
れるウェハ14上に供給するガス供給方法を改善し、成
膜される膜厚を均一性を向上させようとしていることを
特徴としている。
Further, in this vapor phase growth apparatus, the direction of gas injection from the gas supply pipe 10 is set to 10 from the axial center of the reaction tube.
By injecting gas while moving in the tube at an angle of 30 ° to 30 °, the method of supplying gas onto the wafer 14 mounted on the susceptor 9 is improved, and the film thickness to be formed is uniform. It is characterized by trying to improve the sex.

【0007】[0007]

【発明が解決しようとする課題】上述した従来の横型反
応装置では、ガス噴射口をもつガス供給管を回転させな
がら移動しガスを供給し膜厚の均一化が図れるものの、
成長膜や不純物拡散によっても、ガスの噴射方向を変え
ななければならず、極めて操作性が悪いという欠点があ
る。また、ガス供給管を管内に移動する機構が必要とな
ることから設備コストが高くなる欠点もある。さらに、
移動しながら旋回する機構が発塵源となり、ウェハの成
膜を汚染させる品質に重大な欠陥をもたらすという問題
がある。
In the above-mentioned conventional horizontal reactor, the gas supply pipe having the gas injection port is moved while being rotated to supply the gas to make the film thickness uniform.
The gas injection direction must be changed even by the growth film and the diffusion of impurities, which has a drawback of extremely poor operability. Further, there is also a drawback that the equipment cost becomes high because a mechanism for moving the gas supply pipe into the pipe is required. further,
There is a problem in that the mechanism that swirls while moving acts as a dust source and causes a serious defect in the quality that contaminates the film formation of the wafer.

【0008】従って、本発明の目的は、発塵源となる複
雑な可動機構を必要とせずウェハの表面処理を均一にで
きる横型反応装置を提供することである。
Therefore, an object of the present invention is to provide a horizontal reactor capable of uniformly treating the surface of a wafer without requiring a complicated movable mechanism which is a dust source.

【0009】[0009]

【課題を解決するための手段】本発明の特徴は、横方向
に長尺な炉芯管内に挿入され高温加熱されるとともに反
応ガスの雰囲気のもとで半導体基板を酸化・拡散処理ま
たは多結晶シリコン膜,窒化膜等を成膜する横型反応装
置において、前記炉芯管内の上部に配置されるとともに
前記反応ガスを導入するガス吹き出し口の複数個が横方
向に並べ配設されるガス供給機構と、前記炉芯管内の下
部に前記ガス吹き出し口に対向して配設されるとともに
前記反応ガスを排気するガス排気口を具備するガス排出
管とを備える横型反応装置である。また、前記ガス供給
機構は、前記ガス吹き出し口の一つを具備する複数のガ
ス導入管を備えることが望ましい。
A feature of the present invention is that the semiconductor substrate is inserted into a laterally elongated furnace core tube and heated at a high temperature, and the semiconductor substrate is oxidized / diffused or polycrystallized under an atmosphere of a reaction gas. In a horizontal reactor for depositing a silicon film, a nitride film, etc., a gas supply mechanism arranged in the upper part of the furnace core tube and having a plurality of gas outlets for introducing the reaction gas arranged side by side in the lateral direction. And a gas discharge pipe having a gas exhaust port that is disposed in the lower part of the furnace core tube so as to face the gas outlet port and that exhausts the reaction gas. Further, it is preferable that the gas supply mechanism includes a plurality of gas introduction pipes having one of the gas outlets.

【0010】[0010]

【発明の実施の形態】次に、本発明について図面を参照
して説明する。
Next, the present invention will be described with reference to the drawings.

【0011】図1(a)および(b)は本発明の一実施
の形態における横型反応装置を示す模式縦断面図および
模式横は横断面図である。この横型反応装置は、図1に
示すように、炉芯管6内の上部に配置されるとともに前
記反応ガスを導入するガス吹き出し口3a,3b,3c
の複数個が横方向に並べ配設されるガス供給機構1と、
炉芯管内の下部にガス吹き出し口3a,3b,3cに対
向して配設されるとともに反応ガスを排気するガス排気
口4を具備するガス排出管2とを設けたことである。そ
れ以外は、図2で説明した従来の横型反応装置と同じで
ある。
1A and 1B are a schematic vertical sectional view and a schematic horizontal sectional view, respectively, showing a horizontal reactor in one embodiment of the present invention. This horizontal reactor is, as shown in FIG. 1, arranged in the upper part of the furnace core tube 6 and has gas outlets 3a, 3b, 3c for introducing the reaction gas.
A plurality of gas supply mechanisms 1 arranged side by side in the lateral direction,
The gas discharge pipe 2 is provided in the lower part of the furnace core tube so as to face the gas outlets 3a, 3b, 3c and has a gas exhaust port 4 for exhausting the reaction gas. Other than that, it is the same as the conventional horizontal reactor described in FIG.

【0012】ガス供給機構1は、複数のガス導入管1
a,1b,1cで構成され、ガス吹き出し口3a,3
b,3cでの反応ガスの流量が一定になるように、それ
ぞれのガス導入管1a,1b,1cには独立して流量弁
(図示せず)が設けられている。また、ガス吹き出し口
3a,3b,3cは、ボート5に並べ載置されたウェハ
14に一様に供給されるように、長手方向に等間隔に配
置されている。
The gas supply mechanism 1 includes a plurality of gas introduction pipes 1.
a, 1b, 1c, and gas outlets 3a, 3
Flow rate valves (not shown) are independently provided in the respective gas introduction pipes 1a, 1b, 1c so that the flow rates of the reaction gases in b, 3c become constant. The gas outlets 3a, 3b, 3c are arranged at equal intervals in the longitudinal direction so that the gas is uniformly supplied to the wafers 14 placed side by side on the boat 5.

【0013】一方、炉芯管6の下部には、ガス吹き出し
口3a,3b,3cのそれぞれに対向してガス排気口4
をもつガス排出管2が配設されている。ボート5のウェ
ハ14の間を層流の状態で反応ガスを一様に流し、常
に、活性分子を多く含む新鮮で濃度が一様な反応ガスを
ウェハ14に接触させている。また、より流れを一様に
するためには、このガス排出管2を各排気口4を独立し
てもつ分岐配管にし、これら分岐された配管に排気抵抗
を調節できる調節弁を設け、それぞれを調節し、ウェハ
14の間の流れを一様にすれば良い。
On the other hand, at the lower part of the furnace core tube 6, the gas exhaust port 4 is provided so as to face the gas outlets 3a, 3b and 3c.
A gas exhaust pipe 2 having the above is arranged. The reaction gas is made to flow uniformly in a laminar flow state between the wafers 14 of the boat 5, and a fresh reaction gas having a large concentration of active molecules and having a uniform concentration is constantly brought into contact with the wafer 14. In order to make the flow more uniform, the gas discharge pipe 2 is made into a branch pipe having each exhaust port 4 independently, and a control valve capable of adjusting exhaust resistance is provided in each of these branched pipes. It may be adjusted to make the flow between the wafers 14 uniform.

【0014】次に、この横型反応装置の動作手順を説明
する。まず、扉7を開け、高温加熱された炉芯管6内の
ウェハ14を装填した石英製のボート5を挿入する。次
に、扉7を閉じ、炉芯管6の上部に設けられたガス導入
管1a,1b,1cのガス吹き出し口3a,3b,3c
より所望のガス(酸素,窒素等)を導入しながら、ガス
排出管4のガス排気口4より導入された反応ガスを排気
する。このことによりウェハ14は常に濃度の一定の反
応ガスと接触し、ウェハ14の表面を酸化したり、膜成
長したりすることができる。
Next, the operation procedure of this horizontal reactor will be described. First, the door 7 is opened, and the quartz boat 5 loaded with the wafers 14 in the furnace core tube 6 heated at high temperature is inserted. Next, the door 7 is closed, and the gas outlets 3a, 3b, 3c of the gas introduction pipes 1a, 1b, 1c provided on the upper part of the furnace core pipe 6 are closed.
While introducing a more desired gas (oxygen, nitrogen, etc.), the reaction gas introduced through the gas exhaust port 4 of the gas exhaust pipe 4 is exhausted. As a result, the wafer 14 is always in contact with the reaction gas having a constant concentration, and the surface of the wafer 14 can be oxidized or the film can be grown.

【0015】ここで、図面では、炉芯管6の上部のガス
吹き出し口に対向して3箇所の排気口4を示している
が、配置が許される限り3個以上設けても良い。これに
より反応ガスは炉芯管の上部から下部へ層流状態で炉芯
管6の長手方向に対し円滑に流れ、すべてのウェハ14
に対し、一様にガスを供給することができる。その結
果、炉芯管6内で反応にかかわるガスの濃度を均一にす
ることができ、炉芯管内に挿入された半導体基板上に酸
化もしくは成長される膜のバッチ内均一性,面内均一性
を向上させることができる。
Here, in the drawing, three exhaust ports 4 are shown facing the gas outlets in the upper part of the furnace core tube 6, but three or more exhaust ports 4 may be provided as long as the arrangement is permitted. As a result, the reaction gas smoothly flows in the longitudinal direction of the furnace core tube 6 in a laminar flow state from the upper part of the furnace core tube to all the wafers 14
However, the gas can be uniformly supplied. As a result, the concentration of the gas involved in the reaction can be made uniform in the furnace core tube 6, and the in-batch uniformity and the in-plane uniformity of the film that is oxidized or grown on the semiconductor substrate inserted in the furnace core tube. Can be improved.

【0016】また、炉芯管の上部に設けられたガス導入
管1a,1b,1cは、炉の奥,中央,手前側でガスの
吹き出し量をさらに均一化するために、配置が許される
限り、前述の排気口4と同様に炉の奥,中央,手前にそ
れぞれ吹き出し口を持った3本以上の方が望ましい。
Further, the gas introduction pipes 1a, 1b, 1c provided on the upper part of the furnace core tube are arranged as long as the arrangement is allowed in order to further equalize the amount of gas blown out in the back, center and front side of the furnace. As with the above-described exhaust port 4, it is preferable to have three or more blowout ports at the back, center, and front of the furnace.

【0017】[0017]

【発明の効果】以上説明したように本発明は、炉芯管の
上部に配置されるとともに複数枚並べられたウェハの列
にわたり反応ガスを噴出する複数のガス吹き出し口と、
この吹き出し口に対向して炉芯管下部に複数の排気口と
を設け、上方から下方への反応ガスの流れを層流状態で
流すことにより、ウェハのそれぞれは均一の濃度の反応
ガスと接触し、ウェハの表面処理が均一にできるという
効果がある。
As described above, the present invention is provided with a plurality of gas outlets for ejecting a reaction gas over the row of a plurality of wafers arranged on the upper part of the furnace core tube.
A plurality of exhaust ports are provided in the lower part of the furnace core tube facing the blowout port, and the reaction gas flows from the upper side to the lower side in a laminar flow state, so that each of the wafers comes into contact with the reaction gas having a uniform concentration. However, there is an effect that the surface treatment of the wafer can be made uniform.

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

【図1】本発明の一実施の形態における横型反応装置を
示す模式縦断面図および模式横は横断面図である。
FIG. 1 is a schematic vertical sectional view and a schematic horizontal sectional view showing a horizontal reactor according to an embodiment of the present invention.

【図2】従来の横型反応装置の一例を示す模式断面図で
ある。
FIG. 2 is a schematic cross-sectional view showing an example of a conventional horizontal reactor.

【図3】従来の横型反応装置の他の例を示す縦断面図お
よび横断面図である。
FIG. 3 is a longitudinal sectional view and a lateral sectional view showing another example of a conventional horizontal reactor.

【符号の説明】[Explanation of symbols]

1 ガス供給機構 1a,1b,1c ガス導入管 2 ガス排出管 3a,3b,3c ガス吹き出し口 4 ガス排気口 5,13 ボート 6,11 炉芯管 7 扉 10 ガス供給管 11a 反応管 12 ヒータ 14 ウェハ 1 gas supply mechanism 1a, 1b, 1c gas introduction pipe 2 gas discharge pipes 3a, 3b, 3c gas outlet 4 gas exhaust 5,13 boat 6,11 furnace core pipe 7 door 10 gas supply pipe 11a reaction pipe 12 heater 14 Wafer

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 横方向に長尺な炉芯管内に挿入され高温
加熱されるとともに反応ガスの雰囲気のもとで半導体基
板を酸化・拡散処理または多結晶シリコン膜,窒化膜等
を成膜する横型反応装置において、前記炉芯管内の上部
に配置されるとともに前記反応ガスを導入するガス吹き
出し口の複数個が横方向に並べ配設されるガス供給機構
と、前記炉芯管内の下部に前記ガス吹き出し口に対向し
て配設されるとともに前記反応ガスを排気するガス排気
口を具備するガス排出管とを備えることを特徴とする横
型反応装置。
1. A semiconductor substrate is subjected to an oxidation / diffusion process or a polycrystalline silicon film, a nitride film or the like is formed under a reaction gas atmosphere while being inserted into a furnace core tube that is long in the lateral direction and heated at a high temperature. In a horizontal reactor, a gas supply mechanism arranged in an upper part in the furnace core tube and a plurality of gas outlets for introducing the reaction gas arranged side by side in a lateral direction, and a gas supply mechanism arranged in a lower part in the furnace core tube. A horizontal reaction apparatus, comprising: a gas exhaust pipe, which is provided so as to face a gas outlet and has a gas exhaust port for exhausting the reaction gas.
【請求項2】 前記ガス供給機構は、前記ガス吹き出し
口の一つを具備する複数のガス導入管を備えることを特
徴とする請求項1記載の横型反応装置。
2. The horizontal reactor according to claim 1, wherein the gas supply mechanism includes a plurality of gas introduction pipes each having one of the gas outlets.
JP30533695A 1995-11-24 1995-11-24 Lateral reactor Pending JPH09148259A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30533695A JPH09148259A (en) 1995-11-24 1995-11-24 Lateral reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30533695A JPH09148259A (en) 1995-11-24 1995-11-24 Lateral reactor

Publications (1)

Publication Number Publication Date
JPH09148259A true JPH09148259A (en) 1997-06-06

Family

ID=17943893

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30533695A Pending JPH09148259A (en) 1995-11-24 1995-11-24 Lateral reactor

Country Status (1)

Country Link
JP (1) JPH09148259A (en)

Cited By (10)

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KR100436084B1 (en) * 2001-11-12 2004-06-12 주식회사 크레젠 Horizontal type Diffusion Furnace for manufacturing semiconductor wafer
JP2012009641A (en) * 2010-06-25 2012-01-12 Koyo Thermo System Kk Continuous diffusion processing apparatus
JP2012009638A (en) * 2010-06-25 2012-01-12 Koyo Thermo System Kk Continuous diffusion processing apparatus
CN103451624A (en) * 2012-05-30 2013-12-18 北大方正集团有限公司 Deposition furnace tube and method for depositing thin films
JP2015188095A (en) * 2015-05-20 2015-10-29 光洋サーモシステム株式会社 Continuous diffusion processing apparatus
JP2015201650A (en) * 2015-05-20 2015-11-12 光洋サーモシステム株式会社 Continuous diffusion processing apparatus
JP2015201651A (en) * 2015-05-20 2015-11-12 光洋サーモシステム株式会社 Continuous diffusion processing apparatus
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US11891692B2 (en) 2017-12-22 2024-02-06 Murata Manufacturing Co., Ltd. Film-forming device

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KR100436084B1 (en) * 2001-11-12 2004-06-12 주식회사 크레젠 Horizontal type Diffusion Furnace for manufacturing semiconductor wafer
JP2012009641A (en) * 2010-06-25 2012-01-12 Koyo Thermo System Kk Continuous diffusion processing apparatus
JP2012009638A (en) * 2010-06-25 2012-01-12 Koyo Thermo System Kk Continuous diffusion processing apparatus
CN103451624A (en) * 2012-05-30 2013-12-18 北大方正集团有限公司 Deposition furnace tube and method for depositing thin films
JP2015188095A (en) * 2015-05-20 2015-10-29 光洋サーモシステム株式会社 Continuous diffusion processing apparatus
JP2015201650A (en) * 2015-05-20 2015-11-12 光洋サーモシステム株式会社 Continuous diffusion processing apparatus
JP2015201651A (en) * 2015-05-20 2015-11-12 光洋サーモシステム株式会社 Continuous diffusion processing apparatus
US10007185B2 (en) 2016-01-05 2018-06-26 Samsung Electronics Co., Ltd. Electron beam lithography method and apparatus
WO2019124099A1 (en) * 2017-12-22 2019-06-27 株式会社村田製作所 Film-forming device
CN111465714A (en) * 2017-12-22 2020-07-28 株式会社村田制作所 Film forming apparatus
JPWO2019124099A1 (en) * 2017-12-22 2020-09-10 株式会社村田製作所 Film deposition equipment
CN111465714B (en) * 2017-12-22 2022-06-28 株式会社村田制作所 Film forming apparatus
US11377731B2 (en) 2017-12-22 2022-07-05 Murata Manufacturing Co., Ltd. Film-forming device
US11891692B2 (en) 2017-12-22 2024-02-06 Murata Manufacturing Co., Ltd. Film-forming device

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