JP2883157B2 - Vertical heat treatment equipment for substrates - Google Patents
Vertical heat treatment equipment for substratesInfo
- Publication number
- JP2883157B2 JP2883157B2 JP10847790A JP10847790A JP2883157B2 JP 2883157 B2 JP2883157 B2 JP 2883157B2 JP 10847790 A JP10847790 A JP 10847790A JP 10847790 A JP10847790 A JP 10847790A JP 2883157 B2 JP2883157 B2 JP 2883157B2
- Authority
- JP
- Japan
- Prior art keywords
- core tube
- furnace core
- substrate
- gas
- gas flow
- 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 - Fee Related
Links
- 239000000758 substrate Substances 0.000 title claims description 82
- 238000010438 heat treatment Methods 0.000 title claims description 19
- 230000001105 regulatory effect Effects 0.000 claims description 29
- 230000002093 peripheral effect Effects 0.000 claims description 25
- 239000007789 gas Substances 0.000 description 82
- 238000010926 purge Methods 0.000 description 13
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 239000011261 inert gas Substances 0.000 description 6
- 239000010453 quartz Substances 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000005229 chemical vapour deposition Methods 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 239000002516 radical scavenger Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000003028 elevating effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000012495 reaction gas Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 230000009545 invasion Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は、半導体基板、セラミック基板といった各種
の基板に、酸化、アニーリング、CVD(化学気相成
長)、あるいは、拡散などの各種熱処理を行う基板用縦
型熱処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention performs various heat treatments such as oxidation, annealing, CVD (chemical vapor deposition), and diffusion on various substrates such as semiconductor substrates and ceramic substrates. The present invention relates to a vertical heat treatment apparatus for a substrate.
<従来の技術> この種の基板用縦型熱処理装置では、炉芯管に対する
基板ボートの挿脱時や基板ボートを抜き出した状態にお
いて、その炉芯管内に外気が侵入すると、基板を保持し
た基板ボートを炉芯管内に挿入して熱処理を行うとき
に、例えば、酸素供給量の制御が不能になるなど、基板
ボートに保持された基板上の自然酸化膜の成長を助長し
たり、外気中の炭酸ガスなどの不純物が基板に付着する
など、酸化やCVDプロセスなどに悪影響を及ぼす問題が
あった。<Prior Art> In this type of vertical heat treatment apparatus for a substrate, when outside air enters the furnace core tube when the substrate boat is inserted into or removed from the furnace core tube or when the substrate boat is extracted, the substrate holding the substrate is held. When the heat treatment is performed by inserting the boat into the furnace core tube, for example, it becomes impossible to control the amount of supplied oxygen, or promote the growth of a natural oxide film on the substrate held by the substrate boat, or There has been a problem that impurities such as carbon dioxide gas adhere to the substrate and adversely affect oxidation and CVD processes.
そこで、従来では、炉芯管内への外気の侵入を防止す
るために、次のような構成が採用されている。Therefore, conventionally, the following configuration has been adopted in order to prevent outside air from entering the furnace core tube.
A.第1従来例 基板ボート挿脱用の開口の水平方向外側に、開口を囲
む環状の排気口を設け、炉芯管内へN2ガス等の不活性ガ
スを導入して、前記開口から流れ出る不活性ガスととも
に、炉芯管内へ侵入しようとする外気を前記環状の排気
口から排気するように構成する。A. First Conventional Example An annular exhaust port surrounding the opening is provided horizontally outside the opening for inserting and removing the substrate boat, an inert gas such as N 2 gas is introduced into the furnace core tube, and flows out from the opening. Along with the inert gas, outside air that is going to enter the furnace core tube is exhausted from the annular exhaust port.
B.第2従来例 横型タイプではあるが、特開昭61−288415号公報に開
示されているように、反応管の基板ボートを出入する開
放端において、管軸芯と直角な全方角から管軸芯へ向け
て不活性ガスを吹き出してエアーカーテンを形成し、こ
のエアーカーテンによって反応管の内部と外部とを仕切
り、外気が反応管内に侵入することを防止している。B. Second Conventional Example Although it is a horizontal type, as disclosed in Japanese Patent Application Laid-Open No. 61-288415, a tube is formed at an open end of a reaction tube in and out of a substrate boat from all directions perpendicular to the tube axis. An inert gas is blown toward the axis to form an air curtain, and the air curtain partitions the inside and outside of the reaction tube, thereby preventing outside air from entering the inside of the reaction tube.
<発明が解決しようとする課題> しかしながら、第1および第2の従来例のいずれの場
合にも次のような欠点があった。<Problems to be solved by the invention> However, both of the first and second conventional examples have the following disadvantages.
a.第1従来例の欠点 炉芯管内へ導入される不活性ガスが炉芯管の管軸芯お
よびその近辺では高速で吹き出されるが、炉芯管の内周
面近辺では圧力が低下して負圧になり、外気が炉芯管内
に侵入してしまう欠点があった。a. Disadvantages of the first conventional example The inert gas introduced into the furnace core tube is blown out at high speed in and around the furnace core of the furnace core tube, but the pressure decreases near the inner peripheral surface of the furnace core tube. As a result, there is a drawback that the air becomes negative pressure and the outside air enters the furnace core tube.
また、環状の排気口からの吸い込みが、環状の排気口
の全周にわたって均一でなければ、かかる排気口におけ
る比較的吸い込みが弱い部位の近くでは、部分的に気圧
が低くなって、炉芯管内へ外気が流れ込むような気流を
生じ、外気が炉芯管内へ侵入する欠点があった。In addition, if the suction from the annular exhaust port is not uniform over the entire circumference of the annular exhaust port, the air pressure partially decreases near the relatively weakly sucked portion of the exhaust port, and the pressure inside the furnace core tube is reduced. There is a drawback that an airflow is generated such that outside air flows into the furnace core tube and the outside air enters the furnace core tube.
b.第2従来例の欠点 吹き出される不活性ガスが反応管の管軸芯側で互いに
衝突して三次元方向の複雑な流れを発生し、外気を反応
管内に取込む欠点があった。また、基板ボートを出入す
るときにエアーカーテンが消滅して外気が流入しやすい
欠点があった。b. Disadvantages of the second conventional example There is a disadvantage that the blown-in inert gases collide with each other on the tube axis side of the reaction tube to generate a complicated three-dimensional flow and take in outside air into the reaction tube. In addition, there is a disadvantage that the air curtain disappears when entering and exiting the substrate boat, so that outside air easily flows in.
本発明は、このような事情に鑑みてなされたものであ
って、基板ボートを炉芯管内に挿脱する状態、ならび
に、炉芯管から基板ボートを脱した状態のいずれにあっ
ても外気の炉芯管内への侵入を防止できるようにするこ
とを目的とする。The present invention has been made in view of such a situation, and the outside air is provided in any of a state where the substrate boat is inserted into and removed from the furnace core tube and a state where the substrate boat is removed from the furnace core tube. An object of the present invention is to prevent entry into a furnace core tube.
<課題を解決するための手段> 本発明は、上述のような目的を達成するために、基板
に熱処理を行う基板用縦型熱処理装置において、管軸芯
方向が上下方向を向くように設置され、上端側にガスを
供給するためのガス導入孔を設け、下端側に開口を有す
る炉芯管と、前記炉芯管の周囲に設けられた加熱手段
と、前記炉芯管の開口を通して前記炉芯管内に挿脱自在
であって、基板を保持する基板ボートと、前記基板ボー
トが前記炉芯管内にある状態では、前記基板ボートの上
端に載置され、前記炉芯管の内周面との間で環状の隙間
を形成し、前記ガス導入孔から前記炉芯管内へ供給され
たガスを前記環状の隙間において流下させるようにガス
流を規制するガス流規制部材と、前記基板ボートが前記
炉芯管外にある状態では、前記炉芯管の開口の位置にお
いて前記ガス流規制部材を支持するストッパーと、を備
えたことを特徴とするものである。<Means for Solving the Problems> In order to achieve the above-described object, the present invention provides a vertical heat treatment apparatus for performing heat treatment on a substrate, which is installed such that a tube axis direction is directed up and down. A furnace inlet tube provided with a gas introduction hole for supplying gas at the upper end side, an opening at the lower end side, heating means provided around the furnace core tube, and the furnace through an opening of the furnace core tube. A substrate boat that can be inserted into and removed from the core tube and holds the substrate, and in a state where the substrate boat is in the furnace core tube, is mounted on an upper end of the substrate boat and has an inner peripheral surface of the furnace core tube. A gas flow regulating member that regulates a gas flow so that a gas supplied from the gas introduction hole into the furnace core tube flows down in the annular gap, and the substrate boat includes the substrate boat. In a state outside the furnace core tube, the opening of the furnace core tube A stopper for supporting the gas flow regulating member at a position.
<作用> 炉芯管内から基板ボートを挿脱するときには、ガス流
規制部材が基板ボートの上端に載置された状態で基板ボ
ートとともに昇降し、炉芯管内へ導入されたガスは、ガ
ス流規制部材と炉芯管内周面との間に形成される環状の
隙間を流下する。この環状の隙間では、ガスは炉芯管の
周方向の全周において均一な下向きの流れとなって流下
する。そして、ガス流規制部材よりも下でも、そのよう
な周方向に均一な流れのままで、基板ボートや基板と炉
芯管内周面との間に形成される隙間を、ガスは流下す
る。<Operation> When the substrate boat is inserted into and removed from the furnace core tube, the gas flow restricting member is moved up and down together with the substrate boat with the gas flow restricting member placed on the upper end of the substrate boat, and the gas introduced into the furnace core tube is subjected to gas flow restriction. It flows down in an annular gap formed between the member and the inner peripheral surface of the furnace core tube. In the annular gap, the gas flows down in a uniform downward flow over the entire circumference of the furnace core tube. Then, even below the gas flow regulating member, the gas flows down the gap formed between the substrate boat or the substrate and the inner peripheral surface of the furnace core tube while maintaining such a uniform flow in the circumferential direction.
そのため、基板ボートや基板と炉芯管内周面との間の
隙間を上向きに通過するように外気が流れ込むような気
流を生じることはない。Therefore, there is no occurrence of an airflow in which outside air flows upward so as to pass upward through the gap between the substrate boat or the substrate and the inner peripheral surface of the furnace core tube.
なお、基板ボートや基板と炉芯管内周面との間の隙間
よりも管軸側は、気流がなく、また、基板や基板ボート
が上下方向の気流を阻止することもあって、環状の隙間
よりも管軸側を通過して炉芯管内へ流れ込むような外気
の流れは生じない。In addition, there is no airflow on the tube axis side than the gap between the substrate boat or the substrate and the inner peripheral surface of the furnace core tube, and the substrate or the substrate boat may block airflow in the vertical direction. There is no flow of outside air that passes through the tube shaft side and flows into the furnace core tube.
このように、炉芯管内から基板ボートを挿脱するとき
には、炉芯管内へ外気が流れ込むような気流は生じな
い。As described above, when the substrate boat is inserted into or removed from the furnace core tube, an airflow such that outside air flows into the furnace core tube does not occur.
また、炉芯管内から基板ボートを完全に抜き出したと
きには、ガス流規制部材は、ストッパーに支持されて、
炉芯管下端の開口位置にあり、この位置にて、炉芯管内
を流下してきたガスは、ガス流規制部材と炉芯管内周面
との間に形成される環状の隙間を通過する。この環状の
隙間においては、前記のようにガスは炉芯管の周方向の
全周で均一な下向きの流れとなって流下し、この隙間を
上方へ通過するような外気の流れは生じない。そのた
め、炉芯管内から基板ボートを完全に抜き出したとき
も、炉芯管内へ外気が流れ込むような気流は生じない。Further, when the substrate boat is completely extracted from the furnace core tube, the gas flow regulating member is supported by the stopper,
The gas is located at the opening position at the lower end of the furnace core tube, and at this position, the gas flowing down in the furnace core tube passes through an annular gap formed between the gas flow regulating member and the inner peripheral surface of the furnace core tube. In the annular gap, the gas flows down as a uniform downward flow over the entire circumference of the furnace core tube as described above, and there is no flow of outside air passing upward through the gap. Therefore, even when the substrate boat is completely extracted from the furnace core tube, an airflow such that outside air flows into the furnace core tube does not occur.
<実施例> 以下、本発明の実施例を図面に基づいて詳細に説明す
る。<Example> Hereinafter, an example of the present invention will be described in detail with reference to the drawings.
第1実施例 第1図は、基板用縦型熱処理装置の第1実施例の縦断
面図であり、管軸芯方向が上下方向を向くように赤外線
透過性を有する石英材料によって形成された炉芯管本体
1aが設けられ、その炉芯管本体1aの管軸芯方向上端側に
パージガスとしてのN2ガスや反応ガスを供給するガス導
入孔2が設けられ、一方、管軸芯方向下端側に、炉芯管
本体1aと内周面の径が同寸であり、金属製の内筒1bが付
設されている。炉芯管本体1aと内筒1bとが発明の構成に
いう「炉芯管」に相当し、以下、炉芯管本体1aと内筒1b
を炉芯管1と総称する。First Embodiment FIG. 1 is a longitudinal sectional view of a first embodiment of a vertical heat treatment apparatus for a substrate, and a furnace formed of a quartz material having infrared transmittance so that a tube axis direction is directed up and down. Core tube body
1a is provided, and a gas introduction hole 2 for supplying a N 2 gas or a reactive gas as a purge gas is provided at an upper end side of the furnace core tube main body 1a in the tube axis core direction. The diameter of the inner peripheral surface of the core tube main body 1a is the same as that of the core tube main body 1a, and a metal inner cylinder 1b is additionally provided. The furnace core tube main body 1a and the inner cylinder 1b correspond to the “furnace core tube” in the configuration of the present invention, and hereinafter, the furnace core tube main body 1a and the inner cylinder 1b
Are generally referred to as a furnace core tube 1.
なお、内筒1bの下端の開口4から、炉芯管1内へ、お
よび、炉芯管1外へ基板W…を保持した基板ボート3を
挿脱するようになっており、この開口4が発明の構成に
いう「炉芯管の開口」に相当する。The substrate boat 3 holding the substrates W is inserted into and removed from the opening 4 at the lower end of the inner cylinder 1b into the furnace core tube 1 and out of the furnace core tube 1. This corresponds to the “opening of the furnace core tube” in the configuration of the present invention.
ガス導入孔2には、図示しないパージガスの供給手段
と反応ガス供給手段とが選択的に連通接続可能に接続さ
れている。A purge gas supply unit (not shown) and a reactive gas supply unit (not shown) are connected to the gas introduction hole 2 so as to be selectively connected to each other.
前記炉芯管本体1aの周囲に、管軸芯方向に短い第1の
ヒータ5aと長い第2のヒータ5bと短い第3のヒータ5cと
から成る加熱手段5が備えられている。Around the furnace core tube main body 1a, a heating means 5 comprising a first heater 5a, a second heater 5b, and a third heater 5c, which are short in the axial direction of the tube, is provided.
内筒1bの周囲には、排気口6を備えた環状の排気筒7
で形成したスカベンジャー8が設けられ、基板ボート3
を炉芯管本体1aに挿脱したり、基板ボート3を炉芯管本
体1aから抜き出した空状態のときに、ガス導入孔2から
炉芯管本体1a内へ導入され開口4から流出してくるN2ガ
スなどの不活性ガスから成るパージガスとともに、開口
4の周囲の外気を排気口6に排気するように構成されて
いる。An annular exhaust pipe 7 having an exhaust port 6 is provided around the inner cylinder 1b.
A scavenger 8 formed of
Is inserted into and removed from the furnace core tube main body 1a, and when the substrate boat 3 is pulled out of the furnace core tube main body 1a in an empty state, it is introduced into the furnace core tube main body 1a through the gas introduction hole 2 and flows out from the opening 4. The outside air around the opening 4 is exhausted to an exhaust port 6 together with a purge gas composed of an inert gas such as N 2 gas.
また、排気筒7を貫通し、内筒1b内側に開口するよう
に排気管9が設けられ、基板Wを保持した基板ボート3
を炉芯管1内に挿入するとともに、開口4を炉口キャッ
プ10で蓋した状態で純酸素などの反応ガスをガス導入孔
2から流すときに、排気管9から排出していくように構
成されている。Further, an exhaust pipe 9 is provided so as to penetrate the exhaust pipe 7 and open inside the inner pipe 1b, and the substrate boat 3 holding the substrate W is provided.
Is inserted into the furnace core tube 1, and the reaction gas such as pure oxygen is discharged from the gas introduction hole 2 while the opening 4 is covered with the furnace port cap 10, and is discharged from the exhaust pipe 9. Have been.
前記排気口6および排気管9には、図示しない排気手
段が連通接続されている。Exhaust means (not shown) is connected to the exhaust port 6 and the exhaust pipe 9.
基板ボート3は、周方向に間隔を隔てて設けた基板支
持用の石英製で透明の3本の支柱3c…の長手方向両端側
それぞれに石英製の板体3a,3bを一体的に設けて構成さ
れている。The substrate boat 3 is formed by integrally providing quartz plate bodies 3a and 3b on both ends in the longitudinal direction of three transparent support columns 3c made of quartz for substrate support and provided at intervals in the circumferential direction. It is configured.
支柱3c…それぞれには、長手方向に微小ピッチで基板
挿入溝(図示せず)が形成され、基板Wの外縁所要部を
挿入して三点で支持できるように構成されている。Each of the pillars 3c is formed with a substrate insertion groove (not shown) at a minute pitch in the longitudinal direction, and is configured so that a required outer edge of the substrate W can be inserted and supported at three points.
一方(図面上で下方側)の板体3a側には、支柱11…に
断熱板12…を取り付けた断熱支持部材13が設けられてい
る。On one (lower side in the drawing) plate body 3a side, a heat insulating support member 13 in which heat insulating plates 12 are attached to columns 11 is provided.
図中、14は昇降支持アームを示し、この昇降支持アー
ム14を駆動昇降することによって炉口キャップ10を保持
し、その炉口キャップ10上に支持された基板ボート3を
昇降して炉芯管1に挿脱するように構成されている。In the figure, reference numeral 14 denotes an elevating support arm. The elevating support arm 14 is driven up and down to hold the furnace port cap 10, and the substrate boat 3 supported on the furnace port cap 10 is raised and lowered to form a furnace core tube. 1.
第1図、第2図の要部の一部切欠正面図、および、第
3図の要部の斜視図それぞれに示すように、炉芯管1内
に、ガス導入孔2からのガスを炉芯管1の中心から内周
面側に放射状に拡散するキャップ状のガス流規制部材15
が設けられ、一方、炉芯管1を構成する内筒1bの内周面
に、周方向に所定間隔を隔てて、基板ボート3を抜き出
した状態でガス流規制部材15を受け止め支持するストッ
パー16…が付設されている。As shown in a partially cutaway front view of a main part of FIG. 1 and FIG. 2 and a perspective view of a main part of FIG. 3, gas from a gas introduction hole 2 is introduced into a furnace core tube 1. A cap-shaped gas flow regulating member 15 that diffuses radially from the center of the core tube 1 to the inner peripheral surface side
On the other hand, a stopper 16 for receiving and supporting the gas flow regulating member 15 in a state where the substrate boat 3 is pulled out at a predetermined interval in the circumferential direction on the inner peripheral surface of the inner cylinder 1b constituting the furnace core tube 1. … Is attached.
このガス流規制部材15は、例えば、石英のように反応
ガスに冒されない材質によって形成されている。The gas flow restricting member 15 is formed of a material that is not affected by the reaction gas, such as quartz.
基板ボート3の上方側の板体3bには、板体3bを貫通し
た3本の支柱3c…とは別に補助支柱3dが突設され、炉芯
管1内への基板ボート3の挿脱時、ならびに、熱処理時
において、支柱3c…と補助支柱3dとによってガス流規制
部材15を安定支持できるように構成されている。On the plate 3b on the upper side of the substrate boat 3, auxiliary pillars 3d protrude separately from the three pillars 3c penetrating the plate 3b, and when the substrate boat 3 is inserted into and removed from the furnace core tube 1. In addition, at the time of heat treatment, the gas flow restricting member 15 can be stably supported by the columns 3c... And the auxiliary columns 3d.
以上の構成により、炉芯管1内外への基板ボート3の
挿脱時には、ガス導入孔2からのパージガスの供給に伴
い、そのパージガスをガス流規制部材15の上面に衝突さ
せて炉芯管1の内周面側に放射状に拡散するとともに、
ガス流規制部材15の外周、および、基板ボート3の保持
された基板W…それぞれと炉芯管1の内周面との間に形
成される環状の隙間を通じて開口4側に流し、開口4か
ら外部に流出させ、外気を取り込むことなくスカベンジ
ャー8を通じて排出することができる。With the above configuration, when the substrate boat 3 is inserted into and removed from the furnace core tube 1, the purge gas is caused to collide with the upper surface of the gas flow regulating member 15 by supplying the purge gas from the gas introduction hole 2. Radially diffuses into the inner peripheral surface of the
The gas flows toward the opening 4 through an annular gap formed between the outer periphery of the gas flow regulating member 15 and each of the substrates W held on the substrate boat 3 and the inner peripheral surface of the furnace core tube 1. It can be discharged to the outside and discharged through the scavenger 8 without taking in outside air.
一方、炉芯管1内から基板ボート3を抜き出した空状
態のときには、ガス流規制部材15がストッパー16…によ
って受け止め支持され、ガス導入孔2から供給されるパ
ージガスをガス流規制部材15の上面中央部に衝突させて
炉芯管1の内周面側に拡散するとともに、ガス流規制部
材15の外周と内筒1bの内周面との間に形成される環状の
隙間を通じて開口4側に流し、開口4から外部に流出さ
せ、スカベンジャー8を通じて排出することができる。
このとき、開口4に近い位置でガス流規制部材15が開口
4の大部分を蓋し、ガス流規制部材15の外周面と排気筒
7の内筒7bの内周面との間に、炉芯管1の内部空間と外
部とを連通する幅狭で環状の隙間を形成し、ガス流規制
部材15の上面中央部に衝突したパージガスが炉芯管1の
内周面側へ放射状に流れて環状の隙間に流れ込み、この
環状の隙間において、パージガスは炉芯管1の周方向の
全周で均一な下向きの流れとなって流下するから、この
隙間を上方へ通過するような外気の流れは生じない。そ
のため、炉芯管1内から基板ボート3を完全に抜き出し
たときも、炉芯管1内へ流れ込むような気流は生じな
い。On the other hand, when the substrate boat 3 is pulled out of the furnace core tube 1, the gas flow regulating member 15 is received and supported by the stoppers 16. It collides with the central portion and diffuses toward the inner peripheral surface side of the furnace core tube 1, and at the opening 4 side through an annular gap formed between the outer peripheral surface of the gas flow regulating member 15 and the inner peripheral surface of the inner cylinder 1 b. It can be flushed, drained out of the opening 4 and discharged through the scavenger 8.
At this time, the gas flow regulating member 15 covers most of the opening 4 at a position close to the opening 4, and the furnace is located between the outer peripheral surface of the gas flow regulating member 15 and the inner peripheral surface of the inner cylinder 7 b of the exhaust cylinder 7. A purge gas that forms a narrow annular gap communicating the inner space of the core tube 1 with the outside and collides with the center of the upper surface of the gas flow regulating member 15 radially flows toward the inner peripheral surface side of the furnace core tube 1. The purge gas flows into the annular gap, and in this annular gap, the purge gas flows down as a uniform downward flow over the entire circumference of the furnace core tube 1. Does not occur. Therefore, even when the substrate boat 3 is completely extracted from the furnace core tube 1, an airflow that flows into the furnace core tube 1 does not occur.
第2実施例 第4図は、第2実施例のガス流規制部材を示す一部切
欠斜視図であり、ガス流規制部材15が平板で形成されて
いる。Second Embodiment FIG. 4 is a partially cutaway perspective view showing a gas flow regulating member of a second embodiment, in which a gas flow regulating member 15 is formed of a flat plate.
第3実施例 第5図は、第3実施例のガス流規制部材を示す一部切
欠斜視図であり、ガス流規制部材15が、上下を蓋された
円形の箱体で形成されている。Third Embodiment FIG. 5 is a partially cutaway perspective view showing a gas flow restricting member according to a third embodiment, in which a gas flow restricting member 15 is formed of a circular box whose top and bottom are covered.
第4実施例 第6図は、第4実施例のガス流規制部材を示す一部切
欠斜視図であり、ガス流規制部材15が、円形の平板15a
と、その平板15aよりも外周径が小さい円筒15bとから形
成されている。Fourth Embodiment FIG. 6 is a partially cutaway perspective view showing a gas flow restricting member of a fourth embodiment, in which a gas flow restricting member 15 is a circular flat plate 15a.
And a cylinder 15b having a smaller outer diameter than the flat plate 15a.
第5実施例 第7図は、第5実施例のガス流規制部材を示す一部切
欠斜視図であり、ガス流規制部材15のパージガスを衝突
させる上面が、中央部程突出した滑らかな曲面F1に形成
され、ガス流規制部材15の上面に衝突したパージガスを
炉芯管1の内周面側に拡散して流動しやすいように構成
されている。Fifth Embodiment FIG. 7 is a partially cutaway perspective view showing a gas flow regulating member according to a fifth embodiment. The upper surface of the gas flow regulating member 15 against which the purge gas collides has a smooth curved surface F1 protruding toward the center. The purge gas colliding with the upper surface of the gas flow regulating member 15 is configured to be diffused toward the inner peripheral surface side of the furnace core tube 1 and flow easily.
第6実施例 第8図は、第6実施例のガス流規制部材を示す一部切
欠斜視図であり、ガス流規制部材15のパージガスを衝突
させる上面が、中央部の平坦面F2と、その平坦面F2側程
突出した曲面F3とから成る截頭円錐形状に形成され、ガ
ス流規制部材15の上面に衝突したパージガスを炉芯管1
の内周面側に拡散して流動しやすいように構成されてい
る。Sixth Embodiment FIG. 8 is a partially cutaway perspective view showing a gas flow regulating member according to a sixth embodiment. The upper surface of the gas flow regulating member 15 against which the purge gas collides is a flat surface F2 at the center, and The purge gas, which is formed in a truncated cone shape including a curved surface F3 protruding toward the flat surface F2 and colliding with the upper surface of the gas flow regulating member 15, is supplied to the furnace core tube 1.
Is configured to be easily diffused toward the inner peripheral surface side of the device.
第7実施例 第9図は、基板用熱処理装置の別の実施例の縦断面図
であり、第1実施例における炉芯管本体1aを、後述する
外側炉芯管本体20aと内側炉芯管本体20bに替えたもので
あり、第7実施例では外側炉芯管本体20aと内側炉芯管
本体20bおよび内筒1bとが発明の構成にいう「炉芯管」
に相当する。Seventh Embodiment FIG. 9 is a longitudinal sectional view of another embodiment of the substrate heat treatment apparatus. The furnace core tube main body 1a in the first embodiment is replaced by an outer furnace core tube body 20a and an inner furnace core tube described later. In the seventh embodiment, the outer furnace core tube body 20a, the inner furnace core tube body 20b, and the inner cylinder 1b are referred to as "furnace tube" in the seventh embodiment.
Is equivalent to
外側炉芯管本体20aは、円筒面の下部所要箇所にガス
導入口22が形成され、上端がドーム型に閉じられた石英
製の円筒体である。内側炉芯管本体20bは、石英製の円
筒体である。ガス導入口22から外側炉芯管本体20aと内
側炉芯管本体20bとの間の隙間へ導入されたガスは、そ
の隙間の中を上昇して、外側炉芯管本体20aの上端のド
ーム部内で下向きへ流れを変え、基板が収容されている
内側炉芯管本体20b内を流下するように構成されてい
る。The outer furnace core tube main body 20a is a quartz cylindrical body having a gas inlet 22 formed at a required lower portion of a cylindrical surface and an upper end closed in a dome shape. The inner furnace core tube body 20b is a quartz cylindrical body. The gas introduced from the gas inlet port 22 into the gap between the outer furnace core tube body 20a and the inner furnace core tube body 20b rises in the gap, and is in the dome portion at the upper end of the outer furnace core tube body 20a. To change the flow downward and flow down in the inner furnace core tube body 20b in which the substrate is accommodated.
前述第1実施例において、基板ボート3を炉芯管1か
ら抜き出した空状態でガス導入孔2からパージガスを供
給し、炉芯管1内における管軸芯方向での酸素濃度を測
定し、横軸に酸素濃度(ppm)を、縦軸に炉芯管1の管
軸芯方向長さ、すなわち、炉長(mm)をそれぞれとり、
酸素濃度の炉芯管1の管軸芯方向における分布をグラフ
化したところ、第10図のグラフにAで示す結果を得た。In the first embodiment, a purge gas is supplied from the gas introduction hole 2 in an empty state in which the substrate boat 3 has been extracted from the furnace core tube 1, and the oxygen concentration in the tube axis direction in the furnace core tube 1 is measured. The axis is the oxygen concentration (ppm), and the vertical axis is the length of the furnace core tube 1 in the tube axis direction, that is, the furnace length (mm).
When the distribution of oxygen concentration in the furnace core direction of the furnace core tube 1 was graphed, the result indicated by A in the graph of FIG. 10 was obtained.
大気中の酸素濃度は、グラフにBで示すように2×10
5ppmであり、本発明の第1実施例によれば、炉芯管1内
から開口端にわたって酸素濃度が極めて低く、炉芯管1
への外気の侵入を良好に防止できていることが明らかで
あった。The oxygen concentration in the atmosphere was 2 × 10
5 is ppm, according to the first embodiment of the present invention, the oxygen concentration is very low over the open end of core tube within 1, core tube 1
It was clear that the invasion of outside air into the air was successfully prevented.
<発明の効果> 以上説明したように、本発明の基板用縦型熱処理装置
によれば、基板ボートを挿脱する時、ガス流規制部材が
基板ボートの上端に載置された状態にあり、炉芯管内へ
導入されたガスは、ガス流規制部材と炉芯管内周面との
間に形成される環状の隙間を、周方向の全周において均
一な下向きの流れとなって流下し、ガス流規制部材より
も下でも、そのような周方向に均一な流れのままで、基
板ボートや基板と炉芯管内周面との間に形成される環状
の隙間を流下する。そのため、基板ボートや基板と炉芯
管内周面との間の隙間を上向きに通過するように外気が
流れ込むような気流を生じることはない。<Effects of the Invention> As described above, according to the vertical heat treatment apparatus for a substrate of the present invention, when inserting and removing the substrate boat, the gas flow regulating member is placed on the upper end of the substrate boat, The gas introduced into the furnace core tube flows down through the annular gap formed between the gas flow regulating member and the inner peripheral surface of the furnace core tube as a uniform downward flow over the entire circumference in the circumferential direction. Even below the flow restricting member, while maintaining such a uniform flow in the circumferential direction, it flows down in the annular gap formed between the substrate boat or the substrate and the inner peripheral surface of the furnace core tube. Therefore, there is no occurrence of an airflow in which outside air flows upward so as to pass upward through the gap between the substrate boat or the substrate and the inner peripheral surface of the furnace core tube.
また、炉芯管内から基板ボートを完全に抜き出したと
きには、ガス流規制部材は、ストッパーに支持されて、
炉芯管下端の開口位置にあり、この位置にて、炉芯管内
を流下してきたガスは、ガス流規制部材と炉芯管内周面
との間に形成される環状の隙間を、周方向の全周で均一
な下向きの流れとなって流下し、この隙間を上方へ通過
するような外気の流れを生じない。そのため、炉芯管内
から基板ボートを完全に抜き出したときも、炉芯管内へ
外気が流れ込むような気流は生じない。Further, when the substrate boat is completely extracted from the furnace core tube, the gas flow regulating member is supported by the stopper,
At the opening position of the lower end of the furnace core tube, the gas flowing down the furnace core tube at this position passes through an annular gap formed between the gas flow regulating member and the inner peripheral surface of the furnace core tube in the circumferential direction. It flows down as a uniform downward flow over the entire circumference, and does not generate a flow of outside air that passes upward through this gap. Therefore, even when the substrate boat is completely extracted from the furnace core tube, an airflow such that outside air flows into the furnace core tube does not occur.
したがって、炉芯管内への外気の取込みを回避でき、
熱処理時において、酸素供給量の制御を適正に行って酸
化やCVDプロセスなどを良好に行うことができ、品質を
向上できるとともに製品歩留りを高くできるようになっ
た。Therefore, intake of outside air into the furnace core tube can be avoided,
At the time of heat treatment, the oxidation and CVD processes can be performed favorably by properly controlling the oxygen supply amount, so that the quality can be improved and the product yield can be increased.
図面は、本発明に係る基板用縦型熱処理装置の実施例を
示し、第1図は第1実施例の縦断面図、第2図は要部の
一部切欠正面図、第3図は要部の斜視図、第4図は第2
実施例の一部切欠斜視図、第5図は第3実施例の一部切
欠斜視図、第6図は第4実施例の一部切欠斜視図、第7
図は第5実施例の一部切欠斜視図、第8図は第6実施例
の一部切欠斜視図、第9図は、第7実施例の縦断面図で
あり、第10図は第1実施例における酸素濃度の管軸芯方
向の分布を示すグラフである。 1…炉芯管 2…ガス導入孔 3…基板ボート 4…開口 6…排気口 15…ガス流規制部材 16…ストッパー 22…ガス導入口 W…基板The drawings show an embodiment of a vertical heat treatment apparatus for a substrate according to the present invention. FIG. 1 is a longitudinal sectional view of the first embodiment, FIG. 2 is a partially cutaway front view of a main part, and FIG. FIG. 4 is a perspective view of the part, and FIG.
FIG. 5 is a partially cutaway perspective view of the third embodiment, FIG. 6 is a partially cutaway perspective view of the fourth embodiment, FIG.
FIG. 8 is a partially cutaway perspective view of the fifth embodiment, FIG. 8 is a partially cutaway perspective view of the sixth embodiment, FIG. 9 is a longitudinal sectional view of the seventh embodiment, and FIG. It is a graph which shows the distribution of the oxygen concentration in the tube axis direction in an example. DESCRIPTION OF SYMBOLS 1 ... Furnace core tube 2 ... Gas introduction hole 3 ... Substrate boat 4 ... Opening 6 ... Exhaust port 15 ... Gas flow regulating member 16 ... Stopper 22 ... Gas introduction port W ... Substrate
Claims (1)
において、 管軸芯方向が上下方向を向くように設置され、上端側に
ガスを供給するためのガス導入孔を設け、下端側に開口
を有する炉芯管と、 前記炉芯管の周囲に設けられた加熱手段と、 前記炉芯管の開口を通して前記炉芯管内に挿脱自在であ
って、基板を保持する基板ボートと、 前記基板ボートが前記炉芯管内にある状態では、前記基
板ボートの上端に載置され、前記炉芯管の内周面との間
で環状の隙間を形成し、前記ガス導入孔から前記炉芯管
内へ供給されたガスを前記環状の隙間において流下させ
るようにガス流を規制するガス流規制部材と、 前記基板ボートが前記炉芯管外にある状態では、前記炉
芯管の開口の位置において前記ガス流規制部材を支持す
るストッパーと、 を備えたことを特徴とする基板用縦型熱処理装置。1. A vertical heat treatment apparatus for a substrate for performing heat treatment on a substrate, wherein a gas introduction hole for supplying gas is provided at an upper end side, and a gas introduction hole is provided at a lower end side. A furnace core tube having an opening, heating means provided around the furnace core tube, a substrate boat that is insertable into and removable from the furnace core tube through the opening of the furnace core tube, and that holds a substrate; In a state where the substrate boat is in the furnace core tube, the substrate boat is placed on the upper end of the substrate boat and forms an annular gap with the inner peripheral surface of the furnace core tube. A gas flow regulating member that regulates a gas flow so that the gas supplied to the annular gap flows down, and in a state in which the substrate boat is outside the furnace core tube, A stopper for supporting the gas flow regulating member, and Vertical heat treatment device substrate, wherein was e.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10847790A JP2883157B2 (en) | 1990-04-23 | 1990-04-23 | Vertical heat treatment equipment for substrates |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10847790A JP2883157B2 (en) | 1990-04-23 | 1990-04-23 | Vertical heat treatment equipment for substrates |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH045827A JPH045827A (en) | 1992-01-09 |
| JP2883157B2 true JP2883157B2 (en) | 1999-04-19 |
Family
ID=14485750
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10847790A Expired - Fee Related JP2883157B2 (en) | 1990-04-23 | 1990-04-23 | Vertical heat treatment equipment for substrates |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2883157B2 (en) |
-
1990
- 1990-04-23 JP JP10847790A patent/JP2883157B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH045827A (en) | 1992-01-09 |
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