JPS6120318A - Vertical diffusion furnace - Google Patents

Vertical diffusion furnace

Info

Publication number
JPS6120318A
JPS6120318A JP14039684A JP14039684A JPS6120318A JP S6120318 A JPS6120318 A JP S6120318A JP 14039684 A JP14039684 A JP 14039684A JP 14039684 A JP14039684 A JP 14039684A JP S6120318 A JPS6120318 A JP S6120318A
Authority
JP
Japan
Prior art keywords
boat
sub
core
quartz tube
crystal tube
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
JP14039684A
Other languages
Japanese (ja)
Inventor
Toshinobu Yanase
柳瀬 年延
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP14039684A priority Critical patent/JPS6120318A/en
Publication of JPS6120318A publication Critical patent/JPS6120318A/en
Pending legal-status Critical Current

Links

Landscapes

  • Crystals, And After-Treatments Of Crystals (AREA)

Abstract

PURPOSE:To obtain a gentle temperature gradient without making the length of a furnace core longer by providing the subfurnace core part which is movable up and down and surrounds a boat part and by inserting it from the opening end of the furnace core part. CONSTITUTION:The crystal tube 11 as a furnace core tube is placed with directing its opening end downward and the sub-crystal tube 15 which is movable up and down in the crystal tube 11 by a driving device 6 is arranged. The sub-crystal tube 15 is heated by the resistance heating heater 12 with being contained in the crystal tube 11. Next, the sub-crystal tube 15 is lowered to the position where it surrounds a boat 13. At this time, the sub-crystal tube 15 is filled with high-purity gas and subsequently the boat 13 is raised to be put in the crystal tube 11, where it is subjected to heat treatment for the predetermined time. When lowering the sub-crystal tube 15, even though it is lowered at a high speed, crystal defects caused by thermal strain are not produced because of low temperature and the temperature distribution shows gentle temperature gradient which is almost same as that in the case the crystal tube 11 is extended.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は半導体ウェハーを熱処理する縦型拡散炉に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a vertical diffusion furnace for heat treating semiconductor wafers.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

近年、半導体ウェーハが大口径化し、6インチ以上のつ
l−ハも用いられてさらに大口径化されようとしている
。大口径のつI−八を熱処理する場合には、その拡散炉
の炉心管も太くする必要がある。このように炉心管が太
くなると、炉心管を横に置く横型拡散炉の場合、炉心管
が自重により変形Jるおそれがある。また、横型拡散炉
ではダストレベルを低くするため半導体ウェハーを収納
したボートを炉心管にソフトランディングする装置が必
要て゛ある。このため、炉心管の自重による変形が少な
く、ソフトランディング装置の不要な縦型拡散炉が、大
口径の半導体ウェーへの炉として有望である。
In recent years, semiconductor wafers have become larger in diameter, and wafers of 6 inches or more are also being used. When heat treating a large-diameter I-8, the core tube of the diffusion furnace must also be made thicker. When the core tube becomes thick in this way, in the case of a horizontal diffusion furnace where the core tube is placed on the side, there is a risk that the core tube will deform due to its own weight. In addition, in order to lower the dust level in a horizontal diffusion furnace, a device is required for soft landing of a boat containing semiconductor wafers into the reactor core tube. For this reason, a vertical diffusion furnace, in which the core tube is less deformed by its own weight and does not require a soft landing device, is promising as a furnace for large-diameter semiconductor wafers.

第12図に従来の縦型拡散炉を示す。基本的には横型拡
散炉を縦にした構造であり、炉心管である石英管1の周
囲に加熱部である抵抗加熱ヒータ2が設りられている。
FIG. 12 shows a conventional vertical diffusion furnace. Basically, the structure is a vertical diffusion furnace, and a resistance heater 2, which is a heating section, is provided around a quartz tube 1, which is a furnace core tube.

半導体ウェーハを収納したボート3は、駆動部4により
駆動され、石英管1の下端の開口部から挿入される。
The boat 3 containing the semiconductor wafers is driven by the drive unit 4 and inserted through the opening at the lower end of the quartz tube 1 .

抵抗加熱ヒータ2により石英管1が800〜1000℃
の高温に加熱され、石英管1の中央付近は拘熱領域で±
1℃以下の誤差範囲で制御される。しかし石英管1の開
口部を離れると急激に温度が下降する。かかる温度分布
を第13図に示1゜炉に半導体ウェーハを収納しl〔ボ
ート3を挿入する速度は、半導体ウェーハの反りや結晶
欠陥が発生しないような速度でな(ブればならない。こ
の速度はウェーへの口径が大きくなればなるほど遅くす
る必要がある。。ウェーハは通常ボートの進行方向と垂
直に置かれるが、炉から出し入れする場合、ウェーハ周
辺の温度変化が先行し、中心部との間に温度差を生ずる
。この温度差は、ウェーハの口径が大きくなればなるほ
ど大ぎくなり、それだけゆっくりと出し入れする必要が
ある。
The quartz tube 1 is heated to 800 to 1000°C by the resistance heater 2.
The center of the quartz tube 1 is heated to a high temperature of ±
Controlled within an error range of 1°C or less. However, once it leaves the opening of the quartz tube 1, the temperature drops rapidly. Such temperature distribution is shown in FIG. 13. The semiconductor wafer is placed in a 1° furnace and the speed at which the boat 3 is inserted must be such that the semiconductor wafer does not warp or crystal defects occur. The larger the diameter of the wafer, the slower the speed needs to be.The wafer is normally placed perpendicular to the direction of movement of the boat, but when it is taken in and out of the furnace, the temperature change around the wafer precedes the change in temperature between the center and the wafer. The larger the diameter of the wafer, the greater the temperature difference between the wafers and the larger the wafer diameter, and the slower the wafer must be taken in and out.

また温度勾配が急であればそれだけ出し入れの速度はゆ
っくりとしなければならない。温度勾配をゆるやかにす
るには炉心管である石英管の長さを長くすればよいが、
縦型拡散炉では、クリーンルームの天井の高さに限度が
あるため、石英管をそれほど長くすることはできない。
Also, the steeper the temperature gradient, the slower the speed of loading and unloading must be. In order to make the temperature gradient gentler, the length of the quartz tube, which is the furnace core tube, can be made longer.
In a vertical diffusion furnace, the ceiling height of the clean room is limited, so the quartz tube cannot be made very long.

また長くなるとボートの移動距離が長くなり、ボートの
出し入れの時間が長くなってしまう。また温度勾配が急
で挿入速度が遅いと、開口部付近の外気の影響を受け、
ウェーハのフラットバンドボルテージvFBの変動等、
ウェーハ特性が変化するという問題があった。
Also, if the length is longer, the distance the boat must travel will be longer, and the time it will take to load and unload the boat will be longer. Also, if the temperature gradient is steep and the insertion speed is slow, the outside air near the opening will affect the
Fluctuations in wafer flat band voltage vFB, etc.
There was a problem that the wafer characteristics changed.

〔発明の目的〕[Purpose of the invention]

本発明は上記事情を考慮してなされたもので、炉心部の
長さを長くすることはなく、ゆるやかな温度勾配が実現
でき、ウェーハのそりやスリップの発生が防止できる縦
型拡散炉を提供することを目的とする。
The present invention has been made in consideration of the above circumstances, and provides a vertical diffusion furnace that can realize a gentle temperature gradient without increasing the length of the reactor core, and can prevent the occurrence of wafer warping or slipping. The purpose is to

〔発明の概要〕[Summary of the invention]

この発明を達成するために本発明による縦型拡散炉は、
ボート部を包囲し、炉心部の開口端より挿入され、上下
移動可能な副炉心部と、この副炉心部を駆動するa1炉
心駆動部とを備えたことを特徴とする。
In order to achieve this invention, the vertical diffusion furnace according to the present invention comprises:
It is characterized by comprising a sub-core part that surrounds the boat part, is inserted from the open end of the core part, and is movable up and down, and an a1 core drive part that drives the sub-core part.

〔発明の実施例〕[Embodiments of the invention]

本発明の一実施例′による縦型拡散炉を第1図に示1゜
炉心管である石英管11は、開口端を下側に設置される
。この石英管11の周囲には抵抗加熱モータ12が設け
られている。半導体ウェーハが多数収納されたボート1
3は、石英管11の開口端の下に位置している。このボ
ート13はボート駆動装置114により、上下に移動で
きるようになっている。この縦型拡散炉の特徴は、石英
管11内を上下移動可能な副石英管15を備えている点
である。この副石英管15は副石英管駆動装置16によ
り、ボート13とは独立に上下移動することが可能であ
る。本実施例では石英管11および副石英管15の長さ
を600mとし、ボート13を320aとする。ウェー
ハを4.76amピッチで並べるとすれば、最大688
枚セラ−7することができる。
A vertical diffusion furnace according to an embodiment of the present invention is shown in FIG. 1. A quartz tube 11, which is a 1° furnace core tube, is installed with its open end facing downward. A resistance heating motor 12 is provided around this quartz tube 11 . Boat 1 containing many semiconductor wafers
3 is located below the open end of the quartz tube 11. This boat 13 can be moved up and down by a boat drive device 114. A feature of this vertical diffusion furnace is that it is provided with an auxiliary quartz tube 15 that can be moved up and down within the quartz tube 11. This sub-quartz tube 15 can be moved up and down independently of the boat 13 by a sub-quartz tube drive device 16. In this embodiment, the length of the quartz tube 11 and the sub-quartz tube 15 is 600 m, and the length of the boat 13 is 320 a. If the wafers are arranged at a pitch of 4.76am, the maximum
It can be made into 7 sheets.

この縦型拡散炉の使用方法の一興体例を第2図に示す。An example of how to use this vertical diffusion furnace is shown in FIG.

まず副石英管15を石英管11内に収納した位置で抵抗
加熱ヒータ12によりこれら石英管11.12を加熱す
る。半導体ウェーハをボート13に収納し、石英管11
と副石英管12の開口部の下にセットする(第2図(a
))。次に副石英管15を、ボート13を包囲する位置
まで下ケル(tl’+2図(b))。このとき副石英管
12内を高純度ガスで満たし、低い温度にすることが可
能である。したがって副石英管12を下げる場合、高速
で下げても、低温であるので熱歪による結晶欠陥は発生
しない。なぎならウェーへの強度は低温になると飛躍的
に増加するためである。またウェーハを短時間で高純度
ガス雰囲気中に保持できる。
First, the quartz tubes 11 and 12 are heated by the resistance heater 12 at the position where the sub-quartz tube 15 is housed in the quartz tube 11. The semiconductor wafers are stored in the boat 13, and the quartz tube 11
and set it under the opening of the sub-quartz tube 12 (see Fig. 2(a)
)). Next, lower the auxiliary quartz tube 15 to a position surrounding the boat 13 (tl'+2 (b)). At this time, it is possible to fill the inside of the sub-quartz tube 12 with high-purity gas and lower the temperature. Therefore, when lowering the sub-quartz tube 12, even if it is lowered at high speed, crystal defects due to thermal strain will not occur because the temperature is low. This is because the strength of the Naginara wae increases dramatically at low temperatures. Furthermore, the wafer can be held in a high-purity gas atmosphere for a short time.

第2図(b)における温度分布は、石英餘11を延長し
た場合とばば同じになり、第3図に丞すにうなゆるやか
な温度勾配を示す。次にボート13を徐々に上げていく
(第2図(C))が、温度勾配がゆるやかなため比較的
速く上げることがぐきる。ボート13が石英管11内に
入ると、そこで所定時間も熱処理がおこなわれる(第2
図(d))。
The temperature distribution in FIG. 2(b) is the same as when the quartz cap 11 is extended, and shows a much gentler temperature gradient in FIG. 3. Next, the boat 13 is gradually raised (FIG. 2 (C)), but because the temperature gradient is gentle, it can be raised relatively quickly. When the boat 13 enters the quartz tube 11, heat treatment is performed there for a predetermined time (second
Figure (d)).

熱処理が終わり、ボート13を出J揚含、逆に第2図(
b)から第2図(ε1)の順に制御Jればよい。ボート
13が下っても副石英管15ぐ包囲されているので、温
度変化が急激で% <、かつ高純度ガス雰囲気中でV混
返くまぐ冷却Jることb可能どなる。
After the heat treatment was completed, the boat 13 was taken out and transferred to the vessel shown in Figure 2 (
Control J may be performed in the order from b) to FIG. 2 (ε1). Even when the boat 13 is lowered, the sub-quartz tube 15 is surrounded, so the temperature changes rapidly, and it is possible to cool the vessel in a high-purity gas atmosphere.

次にこの縦型拡散炉の使用方法の他の貝体例を第4図に
示す。まず副石英管15を石英管11内に収納した位置
で抵抗加熱モータ12により、これら石英管11.12
を加熱する。半導体ウェーハをボート13に収納し、石
英管11と副石英管15の開口部の下にセットする(第
4図(a))。
Next, FIG. 4 shows another example of how to use this vertical diffusion furnace. First, at the position where the sub-quartz tube 15 is stored in the quartz tube 11, the resistance heating motor 12 is used to heat the quartz tubes 11 and 12.
heat up. A semiconductor wafer is stored in a boat 13 and set under the openings of the quartz tube 11 and the sub-quartz tube 15 (FIG. 4(a)).

次にDj石英管15を、ボート13を包囲する位置まで
下げる(第4図(b))。このときの温度分布は第3図
のようになる。次にボート13を徐々に上げていくわけ
であるが、本具体例では副石英管15も同時に上げてい
く(第4図(C))。副石英管15を同時に上げること
により、ボルト13の熱容量を実質的に増し、高速移動
した際の温度変化をゆるやかにできる。ボート13と陣
1石英管15が石英管11内に入ると、そこで所定時間
熱処理がおこなわれる(第4図(d))。熱処理が終わ
り、ボート13を出す場合は、逆に第4図(d)から第
4図(a)の順に制御する。なお、副石英管15の移動
速度は、ボート13の移動速度、副石英管15およびボ
ート13の熱容量に応じて変化させてもよい。
Next, the Dj quartz tube 15 is lowered to a position surrounding the boat 13 (FIG. 4(b)). The temperature distribution at this time is as shown in FIG. Next, the boat 13 is gradually raised, and in this specific example, the auxiliary quartz tube 15 is also raised at the same time (FIG. 4(C)). By raising the sub-quartz tube 15 at the same time, the heat capacity of the bolt 13 is substantially increased, and temperature changes during high-speed movement can be made gentler. When the boat 13 and the first quartz tube 15 enter the quartz tube 11, heat treatment is performed there for a predetermined time (FIG. 4(d)). When the boat 13 is to be taken out after the heat treatment is completed, control is performed in the reverse order from FIG. 4(d) to FIG. 4(a). Note that the moving speed of the sub-quartz tube 15 may be changed depending on the moving speed of the boat 13 and the heat capacities of the sub-quartz tube 15 and the boat 13.

副石英管15の形状は種々の弯形がrI■能である。The shape of the auxiliary quartz tube 15 can be various curved shapes.

例えば第5図に示すように副石英管15の内側にI艮の
突起物17を設けてもよい。これにより副も英管15内
の高純度ガス流の流れがスムーズになる。また第6図の
示すように副石英管15の内側にリング18を複数本設
けてもよい。これによりガス流を変化させて均一化を図
っている。また第7図に示すように螺旋状の帯19を副
石英管15の内側の流れるガス流が螺旋状の軌道を描い
て流れ、熱の均一化が図れるとともに、ガスが均一に供
給される。また2種類のガスを用いた場合、速やかに均
質な混合かできる。また第8図に示すように副石英管1
5の外側に、螺旋状の帯20を設【プてもよい。これに
より副石英管15と石英管11の間のガス流を制御する
ことができる。
For example, as shown in FIG. 5, an I-shaped protrusion 17 may be provided inside the sub-quartz tube 15. As a result, the flow of high-purity gas inside the secondary tube 15 becomes smooth. Further, as shown in FIG. 6, a plurality of rings 18 may be provided inside the sub-quartz tube 15. This changes the gas flow to make it uniform. Further, as shown in FIG. 7, the gas flow inside the sub-quartz tube 15 flows along a spiral band 19 in a spiral trajectory, thereby making it possible to equalize the heat and uniformly supply the gas. Furthermore, when two types of gas are used, homogeneous mixing can be quickly achieved. In addition, as shown in Fig. 8, the sub-quartz tube 1
A spiral band 20 may be provided on the outside of 5. Thereby, the gas flow between the sub-quartz tube 15 and the quartz tube 11 can be controlled.

また副石英管15、ボート13を上下移動するたりてな
く、回転させるようにしてもよい。これにより熱の均一
化、混合ガスの均質化等がさらに改善される。
Further, the sub-quartz tube 15 and the boat 13 may be rotated instead of being moved up and down. This further improves uniformity of heat, homogenization of mixed gas, etc.

また副石英管15の断面形状を、第9図に示すような4
角形状等他の形状でもよい。また4角形状の閉じた管の
かわりに、第11図に示すように4枚の板で副炉心部1
5を形成してもよい。断面が円形の場合でも、第10図
に示すように閉じた管ではなく2つの半径部材により副
炉心部15を構成するようにしてもよい。
In addition, the cross-sectional shape of the sub-quartz tube 15 is set to 4 as shown in FIG.
Other shapes such as a square shape may also be used. In addition, instead of a closed rectangular tube, four plates are used to form the sub-core part 1, as shown in Figure 11.
5 may be formed. Even when the cross section is circular, the auxiliary core section 15 may be constructed of two radial members instead of a closed tube, as shown in FIG.

副石英管15と石英管11とは密接するようにしてもよ
い。また副石英管15とボート13を密着させてもよい
。また必要に場合には副石英管15に間口部を設けても
よい。
The sub-quartz tube 15 and the quartz tube 11 may be brought into close contact with each other. Further, the sub-quartz tube 15 and the boat 13 may be brought into close contact with each other. Further, if necessary, the sub-quartz tube 15 may be provided with a frontage.

また副石英管を複数にしてそれぞれを独立駆動させても
よい。熱容量正確な調査が可能である。
Alternatively, a plurality of sub-quartz tubes may be provided and each may be driven independently. Accurate investigation of heat capacity is possible.

なお、炉心部および副炉心部の材料としては6英以外の
材料、例えば多結晶シリコンで作り、不純物による汚染
を防止するようにしてもよい。
Note that the core and sub-core may be made of a material other than 6-III, such as polycrystalline silicon, to prevent contamination by impurities.

また副炉心部に別に高純度ガスを導入するガスラインを
設けるようにしてもよい。
Furthermore, a gas line for introducing high-purity gas may be separately provided in the sub-core.

(発明の効果) 以上の通り本発明によれば、炉心部の長さを長くするこ
となく、ゆるやかな温度勾配が実現できる。したがって
ボートの移動速度を速くしても、つ〕−ハの反りやスリ
ップを生ずることが4cい。
(Effects of the Invention) As described above, according to the present invention, a gentle temperature gradient can be realized without increasing the length of the reactor core. Therefore, even if the speed of movement of the boat is increased, warping and slipping may occur.

また副炉心部を高純瓜ガスで渦た一d−J、うにづれば
、ボートを速やかにI!!¥l純度ガス雰囲気中に入れ
ることが可能であり、外気のWe’ilを受(−Jにク
クツることができる。
In addition, if the sub-core was swirled with high-purity melon gas, the boat would be immediately moved to I! ! ¥l It is possible to put it in a purity gas atmosphere, and it can receive We'il of outside air (-J).

さらに副炉心部の移動達磨を変化さけるようにJれば、
全体の熱容量を制御することができ、ウェーハの温すの
変化を精密に制御できる。
Furthermore, if you avoid changing the movement of the auxiliary core,
The overall heat capacity can be controlled, and changes in wafer heating can be precisely controlled.

さらにまた副炉心部の形状を変化させるJ:うにすれば
、高純度ガスの制御や、ボー1〜形状の変化への対応が
可能である。
Furthermore, by changing the shape of the auxiliary core, it is possible to control high-purity gas and respond to changes in the shape.

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

第1図は本発明の一実施例による縦型拡散炉の#1断面
図、第2図、第4図はそれぞれ同縦型拡散炉の使用方法
の具体例を示づ図、第3図は同縦型拡散炉の温度分布を
示すグラフ、第5図、第6図、第7図、第8図、第9図
、第10図、第11図はそれぞれ同縦型拡散炉の副炉心
部の変形例を示す図、 第12図は従来の縦型拡散炉の縦断面図、第13図は同
縦型拡散炉の温度分布を示すグラフである。 1.11・・・石英管、2.12・・・抵抗加熱ヒータ
、3.13・・・ボート駆IJI装置、15・・・静1
6英管、16・・・副石英管駆動装置。 出願人代理人  猪  股    清 第1圓 第2図 第3図 石英管イ装置(myn) 第4図 第8図 γ Q− 6失言位[!mmJ
Figure 1 is a #1 sectional view of a vertical diffusion furnace according to an embodiment of the present invention, Figures 2 and 4 are diagrams showing specific examples of how to use the vertical diffusion furnace, and Figure 3 is a diagram showing a specific example of how to use the vertical diffusion furnace. Graphs showing the temperature distribution of the vertical diffusion furnace, Figures 5, 6, 7, 8, 9, 10, and 11 are for the sub-core of the vertical diffusion furnace, respectively. FIG. 12 is a vertical cross-sectional view of a conventional vertical diffusion furnace, and FIG. 13 is a graph showing the temperature distribution of the vertical diffusion furnace. 1.11...Quartz tube, 2.12...Resistance heater, 3.13...Boat drive IJI device, 15...Station 1
6 quartz tubes, 16... sub-quartz tube drive device. Applicant's representative Kiyoshi Inomata 1st circle 2nd figure 3rd quartz tube equipment (myn) 4th figure 8th figure γ Q-6 Gaffe [! mmJ

Claims (1)

【特許請求の範囲】 1、一端が開口した炉心部と、この炉心部を加熱する加
熱部と、半導体ウェーハを収納し、上下移動自在のボー
ト部と、このボート部を所定速度で上下駆動するボート
駆動部と、前記ボート部を包囲し、前記炉心部の開口端
より挿入され、上下移動自在の副炉心部と、前記ボート
部の上下移動に応じて前記副炉心部を上下駆動する副炉
心駆動部とを備えた縦型拡散炉。 2、特許請求の範囲1項記載の縦型拡散炉において、前
記副炉心駆動部は前記副炉心部を回転駆動することを特
徴とする縦型拡散炉。 3、特許請求の範囲第1項又は第2項記載の縦型拡散炉
において、前記ボート駆動部は前記ボートを回転駆動す
ることを特徴とする縦型拡散炉。 4、特許請求の範囲第1項乃至第3項のいずれかに記載
の縦型拡散炉において、前記炉心部は石英管であること
を特徴とする縦型拡散炉。 5、特許請求の範囲第1項乃至第4項のいずれかに記載
の縦型拡散炉において、前記ボート部および前記副炉心
部は、前記炉心部の下側の開口端より出し入れすること
を特徴とする縦型拡散炉。
[Scope of Claims] 1. A reactor core with one end open, a heating section for heating the reactor core, a boat section that accommodates semiconductor wafers and is movable up and down, and a boat section that drives the boat up and down at a predetermined speed. a boat driving section; a sub-core section that surrounds the boat section, is inserted into the open end of the core section and is movable up and down; and a sub-core that drives the sub-core section up and down in accordance with the vertical movement of the boat section. Vertical diffusion furnace equipped with a drive unit. 2. The vertical diffusion furnace according to claim 1, wherein the auxiliary core drive section rotationally drives the auxiliary core section. 3. The vertical diffusion furnace according to claim 1 or 2, wherein the boat driving section rotationally drives the boat. 4. A vertical diffusion furnace according to any one of claims 1 to 3, wherein the reactor core is a quartz tube. 5. The vertical diffusion furnace according to any one of claims 1 to 4, wherein the boat part and the auxiliary core part are inserted and taken out from a lower open end of the core part. Vertical diffusion furnace.
JP14039684A 1984-07-06 1984-07-06 Vertical diffusion furnace Pending JPS6120318A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14039684A JPS6120318A (en) 1984-07-06 1984-07-06 Vertical diffusion furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14039684A JPS6120318A (en) 1984-07-06 1984-07-06 Vertical diffusion furnace

Publications (1)

Publication Number Publication Date
JPS6120318A true JPS6120318A (en) 1986-01-29

Family

ID=15267816

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14039684A Pending JPS6120318A (en) 1984-07-06 1984-07-06 Vertical diffusion furnace

Country Status (1)

Country Link
JP (1) JPS6120318A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62157136U (en) * 1986-03-26 1987-10-06
JPS647517A (en) * 1987-06-29 1989-01-11 Nec Corp Heat treatment device for semiconductor substrate
JPH01194415A (en) * 1988-01-29 1989-08-04 Kokusai Electric Co Ltd vertical furnace
JPH02289500A (en) * 1989-04-28 1990-11-29 Toshiba Ceramics Co Ltd Vertical heat-treating furnace
JPH02290490A (en) * 1989-04-28 1990-11-30 Toshiba Ceramics Co Ltd Vertical type heat treatment furnace
JPH04243126A (en) * 1991-01-17 1992-08-31 Mitsubishi Electric Corp Semiconductor manufacturing apparatus and its control method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62157136U (en) * 1986-03-26 1987-10-06
JPS647517A (en) * 1987-06-29 1989-01-11 Nec Corp Heat treatment device for semiconductor substrate
JPH01194415A (en) * 1988-01-29 1989-08-04 Kokusai Electric Co Ltd vertical furnace
JPH02289500A (en) * 1989-04-28 1990-11-29 Toshiba Ceramics Co Ltd Vertical heat-treating furnace
JPH02290490A (en) * 1989-04-28 1990-11-30 Toshiba Ceramics Co Ltd Vertical type heat treatment furnace
JPH04243126A (en) * 1991-01-17 1992-08-31 Mitsubishi Electric Corp Semiconductor manufacturing apparatus and its control method

Similar Documents

Publication Publication Date Title
US5997635A (en) Method for fabricating a single-crystal semiconductor
DE69120193T2 (en) Batch process and device for treating semiconductor wafers
KR100282463B1 (en) Heat treatment equipment and heat treatment boat
US6217663B1 (en) Substrate processing apparatus and substrate processing method
US5458688A (en) Heat treatment boat
US5297956A (en) Method and apparatus for heat treating
US5897311A (en) Support boat for objects to be processed
US6179911B1 (en) Method for manufacturing single crystal
JPH05152224A (en) Rapid heat treatment equipment
US5662469A (en) Heat treatment method
JPS6120318A (en) Vertical diffusion furnace
US5356261A (en) Wafer boat rotating apparatus
JP2668001B2 (en) Heat treatment method and apparatus
US5769944A (en) Vertical gradient freeze and vertical Bridgman compound semiconductor crystal growth apparatus capable of applying axial magnetic field
US9234296B2 (en) Apparatus having heat insulating cylinder with step portion for manufacturing semiconductor single crystal
US5178534A (en) Controlled diffusion environment capsule and system
JPS63278227A (en) Heat treatment equipment
TW202041724A (en) Device and process for growing a semiconductor crystal
US3269820A (en) Method, system and apparatus for processing filament-forming mineral materials
JPH0770495B2 (en) Heat treatment equipment
US3183163A (en) Devices for handling fuel elements in a nuclear reactor
JPH0447956Y2 (en)
CN224034375U (en) The reactor's insulation structure, robotic arms, and process equipment
JPH04243126A (en) Semiconductor manufacturing apparatus and its control method
JP2721242B2 (en) Silicon single crystal pulling method