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JP2570201B2 - Heat treatment furnace - Google Patents
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JP2570201B2 - Heat treatment furnace - Google Patents

Heat treatment furnace

Info

Publication number
JP2570201B2
JP2570201B2 JP6265596A JP26559694A JP2570201B2 JP 2570201 B2 JP2570201 B2 JP 2570201B2 JP 6265596 A JP6265596 A JP 6265596A JP 26559694 A JP26559694 A JP 26559694A JP 2570201 B2 JP2570201 B2 JP 2570201B2
Authority
JP
Japan
Prior art keywords
temperature
heater
tube
heat treatment
treatment furnace
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 - Lifetime
Application number
JP6265596A
Other languages
Japanese (ja)
Other versions
JPH08124868A (en
Inventor
英一 紺野
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 Corp
Original Assignee
NEC 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 NEC Corp filed Critical NEC Corp
Priority to JP6265596A priority Critical patent/JP2570201B2/en
Publication of JPH08124868A publication Critical patent/JPH08124868A/en
Application granted granted Critical
Publication of JP2570201B2 publication Critical patent/JP2570201B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、半導体基板であるウェ
ーハを熱処理し不純物の拡散や薄膜形成など行なう熱処
理炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat treatment furnace for heat-treating a wafer as a semiconductor substrate to diffuse impurities and form a thin film.

【0002】[0002]

【従来の技術】この種の熱処理炉は複数枚のウェーハを
収納し高温で熱処理する一種の電気炉である。特にウェ
ーハに不純物を拡散させる熱拡散を行なう場合は、炉内
の温度を1000°C以上昇温しなければならなかっ
た。しかしながら、大容量の炉内温度を1000°C以
上の温度に昇温したりあるいは低い温度に降温したりす
ることは、昇温時間がかかるばかりか降温時間は自然空
冷のため冷却時間が非常に長くかかっていた。従来、こ
の改善策として昇温速度をより早く立上げするために常
時炉内温度を、例えば、ウェーハを収納する前は常時8
00°C程度にしウェーハの処理時には1200°Cに
昇温させ温度立上げ時間の短縮を図っていた。また、時
間のかかる降温時間を短縮するために冷却方法の提案が
種々なされてきた。
2. Description of the Related Art A heat treatment furnace of this type is a kind of electric furnace for storing a plurality of wafers and performing heat treatment at a high temperature. In particular, when performing thermal diffusion for diffusing impurities into a wafer, the temperature in the furnace had to be raised to 1000 ° C. or more. However, raising or lowering the temperature of a large-capacity furnace to a temperature of 1000 ° C. or higher or lowering the temperature requires not only a long time for heating but also a very long cooling time due to natural air cooling. It took a long time. Conventionally, as an improvement measure, the furnace temperature is constantly set to increase the temperature rising rate faster, for example, always 8 before storing the wafer.
At the time of processing the wafer at about 00 ° C., the temperature was raised to 1200 ° C. to shorten the temperature rise time. In addition, various cooling methods have been proposed in order to reduce the time required for cooling down.

【0003】図2は従来の熱処理炉の一例を示す図であ
る。上述した降温時間を短縮した熱処理炉の一例は特開
昭57一13736号公報に開示されている。この熱処
理炉は、図2に示すように、ウェーハ17を収納する石
英反応管15の外側に配設されアルミナ(Al2 O3 )
を材料とする均熱管13と、この均熱管13を爪18を
介して支える石英外管14と、均熱管13と石英外管1
4との間隙内を矢印に示す方向に空気を送風する送風手
段19を備えている。
FIG. 2 is a diagram showing an example of a conventional heat treatment furnace. An example of the heat treatment furnace in which the above-mentioned temperature decreasing time is shortened is disclosed in Japanese Patent Application Laid-Open No. 57-13736. As shown in FIG. 2, this heat treatment furnace is disposed outside a quartz reaction tube 15 for accommodating a wafer 17 and is made of alumina (Al2 O3).
, A quartz outer tube 14 that supports the heat equalizing tube 13 through claws 18, a heat equalizing tube 13 and a quartz outer tube 1.
An air blowing means 19 for blowing air in the direction shown by the arrow in the gap with the air blower 4 is provided.

【0004】この熱処理炉の処理動作は、まず、800
℃に維持されている熱処理炉の石英反応管15中に大気
巻き込みによる酸化膜成長防止およびウェーハ17の急
激な可熱によるソリ防止のためゆっくりしたスピード、
例えば、2〜3cm/minでボートローダにより複数
のウェーハ17が石英反応管15内に収納される。次
に、ウェーハ17は約40分時間をかけてヒータ16に
より1200℃に昇温され(4〜5℃/min)不純物
拡散処理が行われる。次に、所定時間経過後、ヒータ1
6の流れる電流を遮断し、送風手段19により石英外管
15と均熱管13との間の間隙を空冷することによりウ
ェ一ハ17は均熱管13の存在によって均一に保たれな
がら800℃なる温度にまで低下する。そしてボートロ
ーダで炉内よりウェーハ17を取り出す。
[0004] The processing operation of this heat treatment furnace is firstly 800
Slow speed to prevent oxide film growth due to air entrainment in the quartz reaction tube 15 of the heat treatment furnace maintained at 0 ° C. and to prevent warpage due to rapid heat generation of the wafer 17.
For example, a plurality of wafers 17 are stored in the quartz reaction tube 15 by a boat loader at 2-3 cm / min. Next, the temperature of the wafer 17 is increased to 1200 ° C. by the heater 16 over a period of about 40 minutes (4 to 5 ° C./min), and the impurity diffusion process is performed. Next, after a predetermined time has elapsed, the heater 1
6 is cut off, and the gap between the quartz outer tube 15 and the soaking tube 13 is air-cooled by the blowing means 19 so that the wafer 17 is maintained at a uniform temperature of 800 ° C. by the presence of the soaking tube 13. Down to. Then, the wafer 17 is taken out of the furnace by the boat loader.

【0005】この結果、この熱処理炉では、1200℃
から800℃までの降温時間は40分程度になり、通常
の冷却しないときの降温時間130分に対して1/3に
短縮したことを特徴としていた。
As a result, in this heat treatment furnace, 1200 ° C.
The cooling time from the temperature up to 800 ° C. was about 40 minutes, which was characterized in that it was reduced to 1/3 of the usual cooling time of 130 minutes without cooling.

【0006】[0006]

【発明が解決しようとする課題】上述した従来の熱処理
炉では、800℃に降温する降温時間を短縮させるもの
の次のウェーハ処理時の1200℃まで上げるには約4
0分かかるという欠点がある。また、ヒータの出力制御
をどのような方法で行なっているか不明瞭であるが、通
常、降温開始時にヒータ電流を単に遮断するだけだと、
時間の経過に伴なって温度が下降し800°C以下とな
り、再昇温して1200°Cにし安定させるまでには更
に時間がかかる。また、待ち時間によって下降する温度
が変り、再度昇温する毎に昇温時間がばらつき再現性が
ないという欠点がある。この温度立ち上り時間のばらつ
きはひいては処理時間のばらつきを引起し品質に重大な
欠陥をもたらすことになる。
In the above-mentioned conventional heat treatment furnace, although the time for cooling down to 800.degree. C. is reduced, it takes about 4 to increase to 1200.degree. C. in the next wafer processing.
The disadvantage is that it takes 0 minutes. Also, it is unclear how the heater output is controlled, but usually, if the heater current is simply cut off at the start of the temperature drop,
As the time elapses, the temperature decreases to 800 ° C. or less, and it takes more time until the temperature is raised again to 1200 ° C. and stabilized. In addition, there is a disadvantage that the temperature to be lowered changes depending on the waiting time, and the temperature rise time varies every time the temperature is raised again, and there is no reproducibility. This variation in the temperature rise time will eventually lead to a variation in the processing time, leading to serious defects in quality.

【0007】従って、本発明の目的は、昇温および降温
時間をより短縮し処理能力の向上を図ることができかつ
昇温時間が再現性のある熱処理炉を提供することであ
る。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a heat treatment furnace capable of shortening the time required for raising and lowering the temperature and improving the processing capacity, and having a reproducible temperature raising time.

【0008】[0008]

【課題を解決するための手段】本発明の特徴は、複数の
半導体ウェーハを収納する反応管と、この反応管を包み
外周囲にヒータが配設される均熱管と、この均熱管と前
記反応管との間に介在する空間部に伝熱ガス媒体を供給
し該伝熱ガス媒体を循環させる送風機と、この送風機に
切換えバルブを介して接続されるとともに前記伝熱媒体
を高温に維持し蓄くわえる高温用ガス蓄積槽および前記
伝熱ガス媒体を低温に維持し蓄くわえる低温用蓄積槽
と、前記ヒータの出力制御する温度制御部とを備える熱
処理炉である。
SUMMARY OF THE INVENTION The present invention is characterized in that a reaction tube for accommodating a plurality of semiconductor wafers, a heat equalizing tube surrounding the reaction tube and having a heater disposed around the outside thereof, A blower for supplying a heat transfer gas medium to the space interposed between the pipe and the heat transfer gas medium and circulating the heat transfer gas medium, connected to the blower via a switching valve and maintaining the heat transfer medium at a high temperature for storage; A heat treatment furnace comprising: a high-temperature gas storage tank and a low-temperature storage tank for storing and storing the heat transfer gas medium at a low temperature; and a temperature control unit for controlling the output of the heater.

【0009】また、前記温度制御部は、前記均熱管の温
度を検出し前記ヒータの出力制御する系統と前記ヒータ
自身の温度を検出し前記ヒータの出力制御する系統と含
んでいることが望ましい。
Preferably, the temperature control section includes a system for detecting the temperature of the heat equalizing tube and controlling the output of the heater, and a system for detecting the temperature of the heater itself and controlling the output of the heater.

【0010】[0010]

【実施例】次に本発明について図面を参照して説明す
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, the present invention will be described with reference to the drawings.

【0011】図1(a)および(b)はこの熱処理炉
は、図1(a)に示すように、ヒータ5で囲まれた均熱
管4とボート7に載置されたウェーハ17を収納する反
応内管6との間の空間部6aに伝熱ガス媒体を導入管9
a,9bから送り込み排気管8a,8bから排出し伝熱
ガス媒体を循環させる送風機2と、この送風機の背面側
に接続されるとともに伝熱ガス媒体を高温に維持し蓄積
するリザーバ1bと伝熱ガス媒体を低温に維持し蓄積す
るレザーバ1aと、レザーバ1a,1bの供給配管のい
ずれかと導入管9a,9bと排気管8a,8bに切換え
るバルブ11a,12aおよびバルブ11b,12b
と、熱電対10a,10bにより温度を検出しヒータ5
への電流を制御しヒータ5の加熱出力を調節する温度制
御部10とを備えている。
FIGS. 1 (a) and 1 (b) show the heat treatment furnace, as shown in FIG. 1 (a), which accommodates a soaking tube 4 surrounded by a heater 5 and a wafer 17 placed on a boat 7. The heat transfer gas medium is introduced into the space 6a between the reaction inner pipe 6 and the pipe 9
a, 9b, a blower 2 for circulating the heat transfer gas medium discharged from the exhaust pipes 8a, 8b, a reservoir 1b connected to the back side of the blower for maintaining and storing the heat transfer gas medium at a high temperature and a heat transfer. A reservoir 1a for maintaining and accumulating a gaseous medium at a low temperature, valves 11a, 12a and valves 11b, 12b for switching to one of supply pipes for reservoirs 1a, 1b, introduction pipes 9a, 9b and exhaust pipes 8a, 8b.
And the temperature is detected by the thermocouples 10a and 10b and the heater 5
And a temperature control unit 10 for controlling the electric current to the heater 5 and adjusting the heating output of the heater 5.

【0012】また、ヒータ5の出力を制御する温度制御
部10は、図面には示さないが、均熱管4の温度を熱電
対10aで検出しヒータ5の電流制御する温度制御系と
ヒータ5自身の温度を熱電対10bで検出しヒータ5の
電流制御する温度制御系との2系統に分れている。そし
て、熱電対10aを含む温度制御系統は、均熱管4の温
度を検出しヒータ5の出力を制御し高い温度、例えば、
1200°Cを設定温度とし一般に知られたPID制御
を行なうものである。一方、熱電対10bを含む温度制
御系統は、ヒータ5自身の温度を検出し前記温度より低
い温度、例えば、800°Cに設定しPID制御する。
A temperature control unit 10 for controlling the output of the heater 5 includes a temperature control system for detecting the temperature of the soaking tube 4 with a thermocouple 10a and controlling the current of the heater 5, and the heater 5 itself, though not shown in the drawing. And a temperature control system that controls the current of the heater 5 by detecting the temperature of the heater 5 with the thermocouple 10b. The temperature control system including the thermocouple 10a detects the temperature of the soaking tube 4 and controls the output of the heater 5 to increase the temperature, for example,
A generally known PID control is performed with a set temperature of 1200 ° C. On the other hand, the temperature control system including the thermocouple 10b detects the temperature of the heater 5 itself, sets the temperature to a temperature lower than the temperature, for example, 800 ° C., and performs PID control.

【0013】ここで、伝熱ガス媒体として、例えば、安
価な窒素ガスを用いそれぞれのレザーバ1a,1bに充
填する。レザーバ1aは恒温槽の一種であってチラーユ
ニットを備え常に常温以下(例えば、20°C)の温度
に維持している。そして、バルブ11aと12aを開く
ことにより送風機2で配管を介して空間部6aを循環す
る。一方、リザーバ1bは一種の蓄熱槽であって、容器
の周囲にヒータが巻付けられており、例えば、800°
C程度の温度の窒素ガスが蓄くわえられている。そし
て、バルブ11bと12bを開くことによって空間部6
aに高温窒素ガスを供給し循環する。なお、バルブ11
bとレザーバ1bとの配管は、図面では短かく示してい
るが、実際の配管は長くなるので、配管にヒータ3を巻
き付けることが望ましい。
Here, as the heat transfer gas medium, for example, inexpensive nitrogen gas is used to fill the respective reservoirs 1a and 1b. The reservoir 1a is a kind of constant temperature bath and includes a chiller unit and is always kept at a temperature lower than normal temperature (for example, 20 ° C.). Then, by opening the valves 11a and 12a, the blower 2 circulates through the space 6a via the pipe. On the other hand, the reservoir 1b is a kind of heat storage tank, in which a heater is wound around the container.
Nitrogen gas at a temperature of about C is stored. The space 6 is opened by opening the valves 11b and 12b.
Supply high temperature nitrogen gas to a and circulate. The valve 11
Although the piping between b and the reservoir 1b is shown short in the drawing, the actual piping is long, so it is desirable to wind the heater 3 around the piping.

【0014】次に、図1(b)を参照してこの熱処理炉
の動作を説明する。まず、レザーバ1bからバルブ11
b,12bを介して送られる高温窒素ガスと低温側に切
換えらた温度制御系により、例えば、800°Cの一定
の高い温度に維持された反応内管6内にボート7ととも
にウェーハ17を収納する。勿論、前述したように、大
気巻き込みによる酸化膜防止や反り防止のためボートロ
ーダにより2〜3cm/minのゆっくりしたスピード
でウェーハ17を炉内へ搬送する。
Next, the operation of the heat treatment furnace will be described with reference to FIG. First, the valve 11 from the reservoir 1b
The wafer 17 is stored together with the boat 7 in the reaction inner tube 6 maintained at a constant high temperature of, for example, 800 ° C. by the high temperature nitrogen gas sent through the b and 12b and the temperature control system switched to the low temperature side. I do. Of course, as described above, the wafer 17 is transferred into the furnace at a slow speed of 2 to 3 cm / min by a boat loader in order to prevent an oxide film and warpage due to entrainment in the atmosphere.

【0015】次に、ウェーハ17の挿入に10分経過し
てt1のとき、温度制御系が熱電対10aを含む高温側
に切換えられヒータ5に前の温度制御系に比べ大電流が
流れる。そして、熱電対10aは常に温度を検出し反応
内管6内の温度を1200°Cになるようにヒータ5に
電流を供給する。このことにより、800°Cで送られ
た窒素ガスは1200°C以上加熱され反応内管6に熱
伝達し反応内管6の内部温度が1200°Cとなる。ち
なみに昇温時間t1〜t2を計測したところ20分であ
った。
Next, at time t1 after 10 minutes have passed since the wafer 17 is inserted, the temperature control system is switched to the high temperature side including the thermocouple 10a, and a larger current flows through the heater 5 than in the previous temperature control system. Then, the thermocouple 10a always detects the temperature and supplies a current to the heater 5 so that the temperature in the inner reaction tube 6 becomes 1200 ° C. As a result, the nitrogen gas sent at 800 ° C. is heated to 1200 ° C. or more and heat is transferred to the inner reaction tube 6, and the internal temperature of the inner reaction tube 6 becomes 1200 ° C. By the way, it was 20 minutes when the heating time t1 to t2 was measured.

【0016】次に、t2からt3までの処理時間は高温
側の温度制御系で1200°Cに一定温度に維持しウェ
ーハ17の不純物拡散を行なう。なお、1200°C以
上に加熱された窒素ガスは排気管8a,8bから排出さ
れ長い配管経路を通してレザーバ1bに戻る。このとき
の窒素ガスは長い配管経路を通過している中に800°
C以下に冷却されている。
Next, the processing time from t2 to t3 is maintained at a constant temperature of 1200 ° C. by the temperature control system on the high temperature side, and the impurity of the wafer 17 is diffused. The nitrogen gas heated to 1200 ° C. or more is exhausted from the exhaust pipes 8a and 8b and returns to the reservoir 1b through a long piping path. The nitrogen gas at this time is 800 ° while passing through a long piping route.
It is cooled below C.

【0017】次に、処理時間が経過しt3になると、バ
ルブ11bとバルブ12bが閉じ代りにバルブ11aと
12aが開きリザーバ1aから常温以下の低温の窒素ガ
スが循環する。この動作と同時にヒータ5への電流を遮
断する。このことにより反応内管6は冷却されt4時間
でほぼ800°Cになる。t4以降は、温度制御系が低
温側に切替えられるとともにバルブ11b,12bが開
き高温の窒素ガスが空間部6aに供給され循環する。こ
のことによりヒータ5は800°C以上上らず一定の温
度を維持し、一方、空間部6a内も800°Cの高温窒
素ガス雰囲気となり反応内管6内の温度は800°Cの
温度で保たれる。
Next, when the processing time elapses and reaches t3, the valves 11a and 12a are opened instead of closing the valves 11b and 12b, and low-temperature nitrogen gas at room temperature or lower circulates from the reservoir 1a. At the same time as this operation, the current to the heater 5 is cut off. As a result, the inner reaction tube 6 is cooled to approximately 800 ° C. in the time t4. After t4, the temperature control system is switched to the low temperature side, and the valves 11b and 12b are opened to supply high-temperature nitrogen gas to the space 6a and circulate. As a result, the temperature of the heater 5 does not rise above 800 ° C., and the heater 5 maintains a constant temperature. On the other hand, the interior of the space 6a also becomes a high-temperature nitrogen gas atmosphere of 800 ° C. Will be kept.

【0018】そして、ウェーハ17を反応内管6より取
出し、未処理のウェーハを再び収納し前述したと同様に
ウェーハの拡散処理を行なう。なお、降温時間を測定し
てみたところ、略30分であり10分程度短縮できた。
また、降温後も温度は下降することなく温度を一定に維
持し、温度の立ち上げ時間および立ち下げ時間が変動な
く常に一定の時間であった。
Then, the wafer 17 is taken out from the inner reaction tube 6, the unprocessed wafer is stored again, and the wafer is diffused in the same manner as described above. In addition, when the temperature lowering time was measured, it was approximately 30 minutes, which could be shortened by about 10 minutes.
Further, even after the temperature was lowered, the temperature was kept constant without lowering, and the rise time and fall time of the temperature were always constant without fluctuation.

【0019】[0019]

【発明の効果】以上説明したように本発明は、ヒータを
外周囲に配設する均熱管とこの均熱管に包まれる反応内
管との間の空間部に反応内管の維持温度に等しい温度の
伝熱ガス媒体を循環しながらヒータ自身の温度を検知し
出力制御を行なうことによって、ウェーハの待ち時間の
長短にかかわらず反応内管の維持温度を常に一定にし、
昇温時には均熱管の温度を検出しヒータの出力を制御し
て一定の維持温度から処理温度まで上げるので、昇温時
間をより早くできしかも昇温時間の再現性が良くなると
いう効果がある。また、処理温度から維持温度まで反応
内管を冷却するのに空間部に常温以下の伝熱ガス媒体を
供給し循環させることにより降温時間を短縮でき処理能
力の向上が図れるという効果もある。
As described above, according to the present invention, the temperature equal to the maintenance temperature of the reaction inner tube is provided in the space between the heat equalizing tube in which the heater is disposed on the outer periphery and the reaction inner tube surrounded by the heat equalizing tube. By controlling the output of the heater by detecting the temperature of the heater itself while circulating the heat transfer gas medium, the maintenance temperature of the reaction inner tube is always kept constant regardless of the length of the waiting time of the wafer,
At the time of temperature rise, the temperature of the soaking tube is detected and the output of the heater is controlled to increase the temperature from a constant maintenance temperature to the processing temperature. Therefore, there is an effect that the temperature rise time can be shortened and the reproducibility of the temperature rise time is improved. Further, by supplying and circulating a heat transfer gas medium having a temperature equal to or lower than the room temperature to cool the inner reaction tube from the processing temperature to the maintenance temperature, there is also an effect that the cooling time can be reduced and the processing capacity can be improved.

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

【図1】本発明の熱処理炉一実施例を示す図および動作
を説明するための温度線図である。
FIG. 1 is a diagram showing an embodiment of a heat treatment furnace of the present invention and a temperature diagram for explaining the operation.

【図2】従来の熱処理炉の一例を示す図である。FIG. 2 is a diagram showing an example of a conventional heat treatment furnace.

【符号の説明】[Explanation of symbols]

1a,1b レザーバ 2 送風機 3,5,16 ヒータ 4,13 均熱管 6 反応内管 6a 空間部 7 ボート 8a,8b 排気管 9a,9b 導入管 10 温度制御部 10a,10b 熱電対 11a,11b,12a,12b バルブ 14 石英外管 15 石英反応管 17 ウェーハ 18 爪 19 送風手段 1a, 1b Reservoir 2 Blower 3,5,16 Heater 4,13 Heat equalizing tube 6 Reaction inner tube 6a Space 7 Boat 8a, 8b Exhaust tube 9a, 9b Inlet tube 10 Temperature control unit 10a, 10b Thermocouple 11a, 11b, 12a , 12b Valve 14 Quartz outer tube 15 Quartz reaction tube 17 Wafer 18 Claw 19 Blowing means

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 複数の半導体ウェーハを収納する反応管
と、この反応管を包み外周囲にヒータが配設される均熱
管と、この均熱管と前記反応管との間に介在する空間部
に伝熱ガス媒体を供給し該伝熱ガス媒体を循環させる送
風機と、この送風機に切換えバルブを介して接続される
とともに前記伝熱媒体を高温に維持し蓄くわえる高温用
ガス蓄積槽および前記伝熱ガス媒体を低温に維持し蓄く
わえる低温用蓄積槽と、前記ヒータの出力制御する温度
制御部とを備えることを特徴とする熱処理炉。
1. A reaction tube for accommodating a plurality of semiconductor wafers, a heat equalizing tube surrounding the reaction tube and having a heater disposed around the reaction tube, and a space interposed between the heat equalizing tube and the reaction tube. A blower that supplies a heat transfer gas medium and circulates the heat transfer gas medium; a high-temperature gas storage tank connected to the blower via a switching valve for maintaining and storing the heat transfer medium at a high temperature; A heat treatment furnace comprising: a low-temperature storage tank that maintains and stores a gas medium at a low temperature; and a temperature control unit that controls output of the heater.
【請求項2】 前記温度制御部は、前記均熱管の温度を
検出し前記ヒータの出力制御する系統と前記ヒータ自身
の温度を検出し前記ヒータの出力制御する系統と含んで
いることを特徴とする請求項1記載の熱処理炉。
2. The temperature control unit includes a system for detecting the temperature of the heat equalizing tube and controlling the output of the heater, and a system for detecting the temperature of the heater itself and controlling the output of the heater. The heat treatment furnace according to claim 1, wherein
JP6265596A 1994-10-28 1994-10-28 Heat treatment furnace Expired - Lifetime JP2570201B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6265596A JP2570201B2 (en) 1994-10-28 1994-10-28 Heat treatment furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6265596A JP2570201B2 (en) 1994-10-28 1994-10-28 Heat treatment furnace

Publications (2)

Publication Number Publication Date
JPH08124868A JPH08124868A (en) 1996-05-17
JP2570201B2 true JP2570201B2 (en) 1997-01-08

Family

ID=17419325

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6265596A Expired - Lifetime JP2570201B2 (en) 1994-10-28 1994-10-28 Heat treatment furnace

Country Status (1)

Country Link
JP (1) JP2570201B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5034138B2 (en) * 2001-01-25 2012-09-26 東京エレクトロン株式会社 Heat treatment method and heat treatment apparatus
JP4149687B2 (en) 2001-07-19 2008-09-10 シャープ株式会社 Heat treatment method

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
特開 平6−260429(JP,A))

Also Published As

Publication number Publication date
JPH08124868A (en) 1996-05-17

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